JP4670036B2 - Coupler for portable powder container - Google Patents
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- JP4670036B2 JP4670036B2 JP2004199987A JP2004199987A JP4670036B2 JP 4670036 B2 JP4670036 B2 JP 4670036B2 JP 2004199987 A JP2004199987 A JP 2004199987A JP 2004199987 A JP2004199987 A JP 2004199987A JP 4670036 B2 JP4670036 B2 JP 4670036B2
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本発明は、移動可能な密閉コンテナに貯蔵した粉粒体を接続先設備に排出するためのカプラーであり、メス型をコンテナの取出し口に接続しておけば、使用場所にてオス型と接合し、空気等の搬送ガスの供給を受け、密閉コンテナ内に貯蔵された粉粒体を連続的に定量排出することが可能であり、且つ、脱着時には粉粒体の漏洩を起こすことのないカプラーに関する。 The present invention is a coupler for discharging a granular material stored in a movable closed container to a connection destination facility. If a female mold is connected to a container outlet, it is joined to a male mold at a place of use. Coupler that can be supplied with carrier gas such as air and can continuously and quantitatively discharge the granular material stored in a sealed container, and does not cause leakage of granular material during desorption About.
ホッパー等に貯蔵された粉粒体を、そこから定量搬送するためには、スクリューフィーダー、振動フィーダー、吸引ノズルなどを用いるとが、これらはいずれも粉粒体の有する流動性に大きく依存する方法であるため、粉粒体をスムーズに流動させることが難しく、排出量がバラツキ、定量排出性を確保することが困難である。 A screw feeder, a vibration feeder, a suction nozzle, etc. are used to quantitatively convey the granular material stored in a hopper, etc., all of which depend greatly on the fluidity of the granular material. Therefore, it is difficult to smoothly flow the granular material, the discharge amount varies, and it is difficult to ensure the quantitative discharge property.
そのため、貯蔵されている粉粒体に搬送用ガスを吹き込み、粉粒体を流動化し、流動層から飛び出した粒子の一部を層上部に設置したプローブにより回収し、後段のプロセスへ排出する動層式定量供給装置が知られており、粒子排出量を変化させるために、プローブ先端位置を上下に移動できるようになっている(図1)。 For this reason, the carrier gas is blown into the stored granular material, the granular material is fluidized, and a part of the particles ejected from the fluidized bed are collected by a probe installed at the upper part of the layer and discharged to the subsequent process. A layer type quantitative supply device is known, and the tip position of the probe can be moved up and down in order to change the particle discharge amount (FIG. 1).
しかし、上記いずれの場合も、輸送用のタンク等からの移送による充填が前提となっているが、そのため、吸湿性、反応性、その他外部と隔離して保存したい粉粒体試料に利用する場合には、パージ等に特別の操作を必要としてきた。 However, in any of the above cases, filling by transfer from a transport tank or the like is premised. Therefore, when using it for hygroscopic, reactive, and other granular samples to be stored separately from the outside However, special operations have been required for purging and the like.
又、凝集性の大きい粉体材料を一次粒子もしくはこれに近い大きさに解離させるとともに、高い定量性を保って次工程に排出することができる粉体排出方法として、粉体材料に旋回流を伴う空気を噴射し、分散された粉体材料を空気とともに吸引して搬送する方法がある。(例えば特許文献1) In addition, as a powder discharge method that dissociates powder material with high cohesiveness into primary particles or a size close to this and discharges it to the next process while maintaining high quantitativeness, a swirling flow is applied to the powder material. There is a method of ejecting the accompanying air and sucking and conveying the dispersed powder material together with the air. (For example, Patent Document 1)
しかしながら、あらかじめ粉粒体が充填したコンテナを利用場所へ移送したのち、コンテナごとに交換できると共に、充填した粉粒体を定量排出せしめる方法は存在していない。 However, there is no method for transferring a container filled with powder in advance to a place of use and then exchanging the container for each container and discharging the filled powder in a fixed amount.
本発明は、従来の粉体定量排出装置とは異なり、移動可能な密閉コンテナに貯蔵された粉粒体を供給する場所に持ち運び、接続先設備から供給される搬送用ガスのみで、コンテナ内の粉粒体を部分流動化し、搬送ガスと共に粉粒体を接続先設備へ、連続に定量排出するためのカプラーである。 Unlike the conventional powder quantitative discharge device, the present invention is carried to a place where the granular material stored in a movable sealed container is supplied, and only the transfer gas supplied from the connection destination facility is used. This is a coupler for partially fluidizing powder particles and continuously discharging the powder particles together with the carrier gas to the connected equipment.
通気抵抗に打ち勝って空間を流れる気体が消費するエネルギーを圧力損失というが、粉粒体が流体のように流動するためには、貯蔵した粉粒体の固定層に搬送ガスを供給し、流量を増大してゆくと、粉粒体を流動化し始める。更に、流量を増加し、粉粒体が流動層となるには、層の圧力損失が層内の単位面積当たりの粉粒体重量に等しくなる状態を作らなければならない。このため、粉粒体の固定層及び流動層の圧力損失、流動化開始速度,粉粒体の終端速度、及び、その時間的変化率が一定の範囲内に制御できることが条件である。 The energy consumed by the gas flowing through the space overcoming the airflow resistance is called pressure loss, but in order for the powder to flow like a fluid, the carrier gas is supplied to the fixed layer of the stored powder and the flow rate is reduced. As it increases, it begins to fluidize the powder. Furthermore, in order to increase the flow rate and the powder becomes a fluidized bed, a state must be created in which the pressure loss of the bed is equal to the weight of the powder per unit area in the bed. For this reason, it is a condition that the pressure loss of the fixed bed and fluidized bed of the granular material, the fluidization start speed, the final speed of the granular material, and the temporal change rate thereof can be controlled within a certain range.
本発明のような、粉粒体の定量排出を目的とした簡易型のカプラーは知られておらず、エアーポンプやコンプレッサーからの空気排出管と、スリットが形成された粉粒体排出管を本発明のカプラーに接続可能とした機器と組合せれば、粉粒体をカートリッジ化した持ち運び可能な商品を使用した新しい市場を開発できる。 There are no known simple couplers for the purpose of quantitative discharge of granular materials, such as the present invention, and an air discharge pipe from an air pump or a compressor and a granular discharge pipe formed with a slit are provided. When combined with the device that can be connected to the coupler of the invention, it is possible to develop a new market using portable products in which powder particles are made into cartridges.
本発明のカプラーの好ましい形状としては細長い円柱形、円錐形または多角柱形あるいは多角錐形等があげられるが、本発明の目的を達成できれば特に限定されない。カプラーを水平面に立てたとき、上端内部には、コンテナ口との接合部(10)、例えば、ネジ山が成型され、カプラーの内部、好ましくは中央部には多孔質プレート(20)が取付けられている。該多孔質プレートは、カプラーの上端と水平に取付けられているのが好ましく、中央に開口部(30)をもち、該多孔質プレートの上側表面一端に固定されたバネの先端に装着されたバルブ(40)によって、前記開口部に密接・閉鎖しており、開閉可能な封止体を構成しており、メス型カプラー(F)をコンテナ口に接続した場合でも、コンテナ内の粉粒体(PW)が漏出することはない。カプラー下端は、粉粒体排出管(P1)、並びに、搬送ガス管(P2)が接合可能な密封構造を保有する可搬粉粒体コンテナ用カプラーであり、可搬粉粒体コンテナの大きさは、タバコケース位の大きさから、サイロのような大きなコンテナに適用が可能である。コンテナにカプラーを接合したのちは、空気、又は、その他の任意の搬送用ガスをエアーポンプやコンプレッサーで供給できれば、どのような場所においても、貯蔵した粉粒体を搬送ガス(G)により接続先設備に定量排出できるカプラーである。カプラーはコンテナとの接合部と多孔質プレート(20)からなるメス型カプラー(F)、並びに、搬送ガス、並びに、粉粒体排出管(P1)が一体となって上記メス型カプラー(F)に密着接合するオス型カプラー(M)のメス型・オス型の分割型カプラーとすれば、工場出荷時にメス型カプラーを装着し、出荷し、受入れ先で、直接オス型カプラーに接続して使用する形態とすることも出来る。 The preferred shape of the coupler of the present invention includes an elongated cylindrical shape, a conical shape, a polygonal column shape, a polygonal pyramid shape, etc., but is not particularly limited as long as the object of the present invention can be achieved. When the coupler stands on a horizontal plane, a joint (10), for example, a thread, is formed inside the upper end, and a porous plate (20) is attached to the inside of the coupler, preferably in the center. ing. The porous plate is preferably mounted horizontally with the upper end of the coupler, and has an opening (30) in the center and a valve attached to the tip of a spring fixed to one end of the upper surface of the porous plate. (40) closes and closes the opening so as to form an openable / closable sealed body, even when the female coupler (F) is connected to the container mouth, PW) will not leak. The lower end of the coupler is a coupler for a portable powder container having a sealed structure to which the powder discharge pipe (P1) and the carrier gas pipe (P2) can be joined. The size of the portable powder container Can be applied to large containers such as silos due to the size of cigarette cases. After the coupler is joined to the container, the stored powder can be connected to the carrier gas (G) at any location as long as air or any other carrier gas can be supplied by an air pump or compressor. It is a coupler that can be discharged quantitatively to equipment. The coupler is a female coupler (F) composed of a junction with a container and a porous plate (20), and the female coupler (F) in which the carrier gas and the granular material discharge pipe (P1) are integrated. If the male coupler (M) is a female coupler / male split coupler that is tightly bonded to the cable, the female coupler is installed at the factory before shipment, shipped, and connected directly to the male coupler for use. It can also be set as a form to do.
本発明のカプラーの詳細な構成と使い方を、メス型、オス型に分割型カプラーを例に説明すると、
(1)粉粒体を可搬粉粒体コンテナ(C)に充填し、充填後、該コンテナの口に本発明のメス型カプラー(F)を接合する。本発明の可搬粉粒体コンテナ用メス型カプラーの接続部(10)はネジ式、フランジ式、クランプ式、あるいは溶接式など、コンテナの大きさ、並びに、用途により密接可能な最適な方式を選択できる。(図2)
The detailed configuration and usage of the coupler of the present invention will be described by taking a split coupler as an example for a female type and a male type.
(1) Fill the portable granular container (C) with the granular material, and after filling, the female coupler (F) of the present invention is joined to the mouth of the container. The connecting part (10) of the female coupler for portable powder container according to the present invention has an optimum method that can be closely connected to the size and application of the container, such as a screw type, a flange type, a clamp type, or a weld type. You can choose. (Figure 2)
(2)可搬粉粒体コンテナ用メス型カプラー内部に開孔部(30)を設けた多孔質プレート(20)が取付けられている。多孔質プレート(20)はリブで補強されていても良い。開口部(30)は弾性のあるプラスチック部材、あるいは、ゴム製Oリングが勘合し、開口部のコンテナ側は、一端を固定したバネ等の弾性体で開口部を圧接・封鎖するための弁が取付けられている。好ましい弁の例としては、バネで圧接されたコーンバルブ(40)がある。弾性体の一端は多孔質プレート(20)面に接合され、固定されている。カプラーを接続すると、コンテナ側の空間(X)は封鎖される。コーンバルブ(40)は下方から押上げられると、移動する、移動する方向としては、どの方向でもよく、押上げがなくなったときには、当初の位置に戻ことが必要である。 (2) The porous plate (20) which provided the opening part (30) inside the female coupler for portable powder container is attached. The porous plate (20) may be reinforced with ribs. The opening (30) is fitted with an elastic plastic member or a rubber O-ring. On the container side of the opening, there is a valve for pressing and sealing the opening with an elastic body such as a spring with one end fixed. Installed. An example of a preferred valve is a cone valve (40) that is pressed by a spring. One end of the elastic body is joined and fixed to the surface of the porous plate (20). When the coupler is connected, the space (X) on the container side is sealed. When the cone valve (40) is pushed up from below, the direction of movement or movement may be any direction. When the push-up is stopped, it is necessary to return to the original position.
(3)可搬粉粒体コンテナ用メス型カプラー(F)のもう一方の端部は、貯蔵されている粉粒体排出管(P1)と、搬送用ガス供給管(P2)から成るオス型カプラーが接合できる構造となっている。例えば、中央部に開口部(50)をもつ円形板が密着し、該開口部(50)周囲は柔軟なプラスチック部材が接合しており、上記管を接合した時点では、該プラスチック部材は管と密接状態となる。メス型カプラー(F)の最外部には、移送時の漏洩や外気の浸入を防止するための漏防防止用フィルム(60)を貼り付けることが好ましい。(図3) (3) The other end of the female coupler (F) for portable powder container is a male type consisting of a stored powder discharge pipe (P1) and a transport gas supply pipe (P2). It has a structure that allows couplers to be joined. For example, a circular plate having an opening (50) is in close contact with the center, and a flexible plastic member is joined around the opening (50). When the pipe is joined, the plastic member is Close state. It is preferable to attach a leakage prevention film (60) for preventing leakage during transfer and intrusion of outside air to the outermost part of the female coupler (F). (Figure 3)
(4)粉粒体排出管(P1)と搬送用ガス供給管(P2)から成るオス型カプラーを、可搬粉粒体コンテナ用メス型カプラーに接続する。粉粒体排出管(P1)は、その先端は密封されてるのが好ましく、先端から一定距離に、四角の窓型や円形或いは楕円形などの形状を保有するスリット(60)が1ヶ所以上形成されている、該スリットの形状および、大きさは、搬送する粉粒体(PW)の物理的形状により適切に決められる。上記管の構造としては、例えば、粉粒体用排出管(P1)が内側に、搬送用ガス管(P2)が外側に形成された同心円構造の二重管とすることもできる。 (4) A male coupler composed of the granular material discharge pipe (P1) and the transport gas supply pipe (P2) is connected to the female coupler for the portable granular container. The tip of the particulate discharge pipe (P1) is preferably hermetically sealed, and at least one slit (60) having a rectangular window shape, a circular shape, an elliptical shape or the like is formed at a certain distance from the tip. The shape and size of the slit are appropriately determined depending on the physical shape of the granular material (PW) to be conveyed. As the structure of the above-mentioned tube, for example, a double tube having a concentric structure in which the powder discharge pipe (P1) is formed on the inner side and the transfer gas pipe (P2) is formed on the outer side can be used.
(5)可搬コンテナを倒置し、メス型にオス型を接合させるため、上記二重管の先端を、開口部(B)に差し込むと、表面の漏防止用フィルム(70)がやぶれ、外管が円形版と蜜接する。内側の粉粒体排出管(P1)を押込むと、粉粒体用排出管(P1)は、開口部(30)に接する。 (5) In order to invert the portable container and join the male type to the female type, when the tip of the double pipe is inserted into the opening (B), the surface leakage prevention film (70) is shattered and removed. The tube is in contact with the round plate. When the inner granular material discharge pipe (P1) is pushed in, the granular material discharge pipe (P1) contacts the opening (30).
(6)粉粒体排出管(P1)を更に押し込むみ、開口部を圧接・封鎖する弁を押上げ、該管のスリット部が多孔質プレート(20)を横切り、ボトル内空間(X)に達する。(図3)このとき、粉粒体排出管(P1)の外周は、開口部(30)に密接している。多孔質プレート(20)としては、金属、又は、プラスチックの微細線からなる網目層を複数積層したもの、あるいは、空隙率の高いセラミック、金属、又は、プラスチック、あるいは、これらの組み合わせからなる多孔質材料を使用したプレートが好ましい。 (6) Push the powder discharge pipe (P1) further, push up the valve that presses and closes the opening, and the slit of the pipe crosses the porous plate (20) to enter the space (X) in the bottle Reach. (FIG. 3) At this time, the outer periphery of the granular material discharge pipe (P1) is in close contact with the opening (30). As the porous plate (20), a plurality of mesh layers made of fine lines of metal or plastic, or a porous material made of ceramic, metal, plastic, or a combination thereof having a high porosity. Plates using materials are preferred.
(7)搬送用ガス(G)の供給を開始し、搬送用ガス(G)を可搬粉粒体コンテナ用カプラーの空間(Y)に流入し、流量調整バルブ(V)を少しずつ開くと、搬送ガスは多孔質プレート(20)を通過し、可搬粉粒体コンテナ側空間(X)の多孔質プレート(20)細孔より搬送ガス(G)を噴射し、コンテナ内の気体は少しずつ粉粒体排出管(P1)のスリット(60)より排出される。搬送用ガスの流量が一定以上になると、噴射された搬送ガス(G)は、カプラー内部に充填された粉粒体(PW)をカプラーの近傍のみで部分的に流動化し流動層(W)を形成し、流動層の一部はスリット(60)から、搬送ガス(G)と同伴して排出されていく。{図4} (7) When the supply of the transfer gas (G) is started, the transfer gas (G) flows into the space (Y) of the coupler for the portable powder container, and the flow rate adjustment valve (V) is opened little by little. The carrier gas passes through the porous plate (20), and the carrier gas (G) is injected from the pores of the porous plate (20) of the portable powder container side space (X). It is discharged from the slit (60) of the granular material discharge pipe (P1) one by one. When the flow rate of the carrier gas exceeds a certain level, the jetted carrier gas (G) partially fluidizes the granular material (PW) filled in the coupler only in the vicinity of the coupler, thereby causing the fluidized bed (W) to flow. A part of the fluidized bed is formed and discharged from the slit (60) together with the carrier gas (G). {Figure 4}
(8)流動しにくく、搬送ガスとの同伴性が劣る、粒径が小さい粉粒体、あるいは、粒径の大きな粒体の場合は、多孔質プレート(20)面に振動板を貼り付け、多孔質プレート(20)を振動させ、強制的に粉粒体(PW)の流動性(W)を増大させることも可能である。 (8) In the case of a granular material having a small particle diameter or a large particle diameter that is difficult to flow and poorly entrained with the carrier gas, a diaphragm is attached to the surface of the porous plate (20), It is also possible to vibrate the porous plate (20) to forcibly increase the fluidity (W) of the granular material (PW).
本発明者らは、粉粒体排出管の挿入位置を調整し、スリット(60)の空間(X)における面積を一定にし、搬送ガス(G)の流量を調整してゆくと、粉粒体(PW)が流動化し始める位置があり、更に、流量を増大させてゆくと、粉粒体が安定した流動層(W)を形成することを見出した。更に、上方空間が密閉されている本発明の条件下では、搬送ガスはスリット(60)のみより排出されるため、スリット(60)に密接している部分からは粉粒体の一部が搬送ガスに同伴され、スリット(60)から排出される様になるが、流動層(W)にはコンテナ上部の固定層の粉粒体(PW)より、減少分がたえず補充されるため流動層(W)領域の大きさは変化なく、又、搬送ガス(G)の流量が一定であると、粉粒体(PW)の排出量も一定であり、流量の増加と共に、直線的に粉粒体の平均流量がほぼ直線的に増加することを見出し、本発明を完成させた。 When the present inventors adjust the insertion position of the granular material discharge pipe, make the area in the space (X) of the slit (60) constant, and adjust the flow rate of the carrier gas (G), the granular material It has been found that there is a position where (PW) starts to fluidize, and further, when the flow rate is increased, the granular material forms a stable fluidized bed (W). Furthermore, since the carrier gas is discharged only from the slit (60) under the condition of the present invention in which the upper space is sealed, a part of the granular material is transported from the portion in close contact with the slit (60). It is entrained by the gas and is discharged from the slit (60), but the fluidized bed (W) is constantly replenished from the granular material (PW) of the fixed layer at the top of the container, so the fluidized bed ( W) The size of the region does not change, and if the flow rate of the carrier gas (G) is constant, the discharge amount of the granular material (PW) is also constant, and the granular material linearly increases as the flow rate increases. As a result, the present invention was completed.
流動層(W)は搬送用ガス(G)に支えられる、つまり、粒子に働く搬送ガス(G)の抗力が粒子の重力とちょうど釣合い、流動層(W)の圧力損失も層内の単位面積あたりの粒子重量に等しくなるため、安定した流動層(W)が形成された状況は(図4)のような、搬送ガス(G)の流出する多孔質プレート(20)とスリット(60)の間の空間部である。 The fluidized bed (W) is supported by the carrier gas (G), that is, the drag force of the carrier gas (G) acting on the particles is just balanced with the gravity of the particles, and the pressure loss of the fluidized bed (W) is also a unit area within the layer. The situation where the stable fluidized bed (W) is formed is equal to the particle weight per particle, as shown in (FIG. 4), between the porous plate (20) through which the carrier gas (G) flows out and the slit (60). It is a space part between.
搬送に必要な標準空気量の目安は、対象とする粉粒体の最小流動化速度に多孔質プレート(20)の面積を乗じた量であり、流量0から本標準流量の2倍程度までの間に定量供給領域が存在する。 The standard amount of standard air required for transportation is the amount obtained by multiplying the minimum fluidization speed of the target granular material by the area of the porous plate (20). From the flow rate 0 to about twice this standard flow rate. There is a fixed supply area in between.
ブロッキングの少ない非付着性粉粒体で径が10μmから5mmの範囲以内であれば、本発明のカプラーを使用し、粒子径に合わせた大きさに搬送ガス量を設定することにより、定量排出が可能である。 If the non-adhesive granular material with less blocking and the diameter is within the range of 10 μm to 5 mm, by using the coupler of the present invention and setting the carrier gas amount to the size according to the particle diameter, quantitative discharge can be achieved. Is possible.
粉炭粒子を貯蔵したコンテナに本発明の粉粒体コンテナ用カプラーのメス型カプラーを接続し、倒置し、取付け口を下側にし、粉炭粒子をボトル空間に充填させ、搬送ガスと粉粒体排出管が一体化されたオス型を接続後、粉粒体排出管を押上げ、スリットを空間に固定する。搬送ガスとして、コンプレッサーより、空気を搬送し、流量調整用バルブで、流量を制御しつつ、ボトル内部で粉粒体の部分流動化状態を現出させる。搬送ガス流量を調整製しながら、一定時間後の粉炭粒子の定在状態において搬送ガス流量と、搬送ガスに同伴される粉炭粒子の平均流量をしらべる。 Connect the female coupler of the powder container coupler of the present invention to the container storing the powdered coal particles, invert, place the mounting port on the bottom, fill the bottle space with the powdered coal particles, discharge the carrier gas and powder particles After connecting the male mold integrated with the tube, the powder particle discharge tube is pushed up to fix the slit in the space. As a carrier gas, air is conveyed from a compressor, and a partially fluidized state of the granular material is caused to appear inside the bottle while controlling the flow rate with a flow rate adjusting valve. While adjusting and producing the carrier gas flow rate, the carrier gas flow rate and the average flow rate of the pulverized coal particles accompanying the carrier gas in the stationary state of the pulverized coal particles after a certain time are examined.
粉炭の微粉末を2リットルの空ペットボトルに充填し、該ペットボトルに本発明の可搬粉粒体コンテナ用メス型カプラーをねじ込み固定する。ペットボトルを倒立し、可搬粉粒体コンテナ用カプラーの開口部に内側に、粉粒体排出管(内径3mm)、外側に搬送ガス排出管の同心二重管から成るカプラーオス型を差込、固定する。粉粒体排出管を押上げ、先端が多孔質プレートの開口部に到達し、更に、強く押込み内管が停止するまで押込む。エアーポンプを稼動し、空気流量をバルブで調整し、粉粒体排出管を上下し、スリットの位置を空間内に固定する。供給する空気流量と内管より空気と同伴される時間当たりの粉炭の流量を測定する。 A fine powder of pulverized coal is filled into a 2 liter empty PET bottle, and the female coupler for portable particle container of the present invention is screwed and fixed to the PET bottle. Invert the plastic bottle and insert a coupler male type consisting of a concentric double pipe with a powder discharge pipe (inner diameter 3 mm) on the inside and a carrier gas discharge pipe on the outside into the opening of the coupler for the portable powder container , Fix. The granular material discharge pipe is pushed up, and is pushed in until the tip reaches the opening of the porous plate and the inner pipe is further stopped. Operate the air pump, adjust the air flow rate with the valve, raise and lower the particulate discharge pipe, and fix the slit position in the space. Measure the flow rate of air supplied and the flow rate of pulverized coal per hour along with air from the inner pipe.
供給する空気流量と粉粒体排出管より排出される粉炭の流量を測定。
搬粉粒体コンテナ用定量排出カプラーを取付けたボトル先端部で粉炭は流動し、排出空気流量増えるほど、空気と同伴される粉炭の流量は増加し、その関係はほぼ直線的に増加し空気流量が一定であれば、同伴される粉炭の流量も一定している。(図5)
Measures the flow rate of air supplied and the flow rate of pulverized coal discharged from the granular material discharge pipe.
The pulverized coal flows at the tip of the bottle attached with the quantitative discharge coupler for the carrier container, and the flow rate of the pulverized coal accompanying the air increases as the exhaust air flow rate increases, and the relationship increases almost linearly. Is constant, the flow rate of entrained pulverized coal is also constant. (Figure 5)
本発明の可搬粉粒体コンテナ用カプラーの別の形態としては、図6及び図7のようにメス型カプラーの多孔質プレート開口部(30)を、閉鎖手段(80)、例えば、弾性の強い菊割れラバーで封止し、搬送ガス管(P2)と粉粒体排出管(P1)が一体となったオス型カプラー(F)をメス型カプラー(M)に嵌合密着する。粉粒体排出管(P1)は中央部に1本(図6)或いは、分岐し、多孔質プレート(20)周辺部に複数の管が挿入可能な開口部(30‘)を保有し{図7}、その先端は角柱、円柱、多角柱、半円形、流線形あるいは、多角錐形等の形状を保有し、その先端近辺には1個以上のスリット(60)を開け、粉粒体排出管(P1)を押上げると、封止体(80)を押上げ、先端部は粉粒体空間(X)に入り込み、管外周は、開口部(30)の柔軟性のあるOリングが密着し、粉粒体(PW)が搬送ガス空間(Y)に漏れ落ちないような形状を保有する、メス型カプラー(F)とオス型カプラー(M)からなる構成のカプラーでもよく、本発明の目的を達成するカプラーであるならば、その構成は上記に限定されるものではない。 As another form of the portable particle container coupler of the present invention, the porous plate opening (30) of the female coupler as shown in FIG. 6 and FIG. Sealed with strong chrysanthemum cracking rubber, and the male coupler (F) in which the carrier gas pipe (P2) and the granular material discharge pipe (P1) are integrated is fitted and adhered to the female coupler (M). The granular material discharge pipe (P1) has one opening (FIG. 6) at the center or a branch, and an opening (30 ′) into which a plurality of pipes can be inserted around the porous plate (20) {FIG. 7}, the tip has a shape such as a prism, cylinder, polygonal column, semi-circle, streamline or polygonal pyramid, and one or more slits (60) are opened in the vicinity of the tip to discharge the granular material. When the pipe (P1) is pushed up, the sealing body (80) is pushed up, the tip part enters the granular material space (X), and the flexible O-ring of the opening part (30) is in close contact with the outer circumference of the pipe. However, it may be a coupler composed of a female coupler (F) and a male coupler (M) having a shape that prevents the powder (PW) from leaking into the carrier gas space (Y). The configuration is not limited to the above as long as the coupler achieves the object.
図8は本発明のカプラーに粉炭を充填したボトルに取り付けた燃料供給装置、図9は、家畜用配合飼料を貯蔵したサイロの運搬車と運搬したサイロに本発明のカプラーを取付け、家畜のえさ台に一定量のえさを排出する装置、図10は、化学工場での反応タンク、粉末原料を定量添加する装置に取り付けた例である。このように、本発明の可搬粉粒体コンテナ用カプラーを使用すれば、粉粒体ハンドリングの手間や、漏洩等のトラブルを招かず、且つ、粉粒体では往々にしてトラブルの多い定量排出を可能とすることができる。 FIG. 8 shows a fuel supply device attached to a bottle filled with pulverized coal in the coupler of the present invention, and FIG. 9 shows a silo carrier vehicle storing livestock feed, and a coupler of the present invention attached to a silo transported to feed livestock. FIG. 10 shows an example in which a fixed amount of food is discharged to a table, and attached to a reaction tank in a chemical factory and a device for quantitatively adding powder raw materials. Thus, if the coupler for portable powder containers of the present invention is used, there is no trouble in handling the powder, or troubles such as leakage, and the powder is often a troublesome quantitative discharge. Can be made possible.
C: コンテナ
F: メス型カプラー
M: オス型カプラー
G: 搬送ガス
PW: 粉粒体
V: 流量調整用バルブ
W: 流動層
P1: 粉粒体排出管
P2: 搬送ガス供給管
10: コンテナ接合部
20: 多孔質プレート
30: 多孔質プレート開口部
40: バルブ
50: 搬送ガス管・粉粒体搬送管接続開口部
60: スリット
70: 漏洩防止フィルム
80: 封鎖手段
C: Container F: Female coupler M: Male coupler G: Carrier gas PW: Powder V: Flow control valve W: Fluidized bed P1: Powder discharge pipe P2: Carrier gas supply pipe 10: Container junction 20: Porous plate 30: Porous plate opening 40: Valve 50: Carrier gas tube / powder particle conveying tube connection opening 60: Slit 70: Leakage prevention film 80: Sealing means
Claims (5)
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JP2004199987A JP4670036B2 (en) | 2004-07-07 | 2004-07-07 | Coupler for portable powder container |
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JP2004199987A JP4670036B2 (en) | 2004-07-07 | 2004-07-07 | Coupler for portable powder container |
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JP2006021859A JP2006021859A (en) | 2006-01-26 |
JP2006021859A5 JP2006021859A5 (en) | 2007-04-12 |
JP4670036B2 true JP4670036B2 (en) | 2011-04-13 |
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JP5181387B2 (en) * | 2008-03-03 | 2013-04-10 | 国立大学法人東京農工大学 | Powder / particle supply coupler, powder / particle supply mechanism using the same, and particle / particle supply system including the mechanism |
CN101966901B (en) * | 2010-10-26 | 2012-05-09 | 太原轨道交通装备有限责任公司 | Tubular bag type fluidized bed device for bulk powder material tank truck |
CN106115093A (en) * | 2016-08-09 | 2016-11-16 | 安徽开乐专用车辆股份有限公司 | A kind of double storehouse is without side stock guide bulk powder goods tanker |
Citations (2)
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JPS56139182A (en) * | 1980-04-02 | 1981-10-30 | Ajikawa Tekko Kensetsu Kk | Coating method of inside surface of metal pipe with resin film |
JP2001187636A (en) * | 1999-12-28 | 2001-07-10 | Tokuyama Corp | Coupling device for discharging powder |
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Patent Citations (2)
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JPS56139182A (en) * | 1980-04-02 | 1981-10-30 | Ajikawa Tekko Kensetsu Kk | Coating method of inside surface of metal pipe with resin film |
JP2001187636A (en) * | 1999-12-28 | 2001-07-10 | Tokuyama Corp | Coupling device for discharging powder |
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