JPS6150848B2 - - Google Patents

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Publication number
JPS6150848B2
JPS6150848B2 JP8438677A JP8438677A JPS6150848B2 JP S6150848 B2 JPS6150848 B2 JP S6150848B2 JP 8438677 A JP8438677 A JP 8438677A JP 8438677 A JP8438677 A JP 8438677A JP S6150848 B2 JPS6150848 B2 JP S6150848B2
Authority
JP
Japan
Prior art keywords
air
pipe
separator
transfer
solids
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
JP8438677A
Other languages
Japanese (ja)
Other versions
JPS5418591A (en
Inventor
Takeshi Hayashi
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Kyoei Zoki Co Ltd
Original Assignee
Kyoei Zoki Co Ltd
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 by Kyoei Zoki Co Ltd filed Critical Kyoei Zoki Co Ltd
Priority to JP8438677A priority Critical patent/JPS5418591A/en
Publication of JPS5418591A publication Critical patent/JPS5418591A/en
Publication of JPS6150848B2 publication Critical patent/JPS6150848B2/ja
Granted legal-status Critical Current

Links

Description

【発明の詳細な説明】 A 産業上の利用分野 本発明は、水等の液体を搬送媒体にして、固形
物を管でもつて立体的に移送する装置に関する。
DETAILED DESCRIPTION OF THE INVENTION A. Field of Industrial Application The present invention relates to an apparatus for three-dimensionally transporting solid materials using a pipe using a liquid such as water as a transport medium.

B 従来の技術 固形物を移送するのに現在最も多用されるもの
はコンベアであるが、コンベアは物を直線的に移
送するものであるから、例えば工場内の機械装置
等の傷害物や通路を避けて立体的にしかも自由に
屈折して搬送することができない欠点がある。
B. PRIOR TECHNOLOGY Conveyors are currently the most commonly used device for transporting solid materials, but since conveyors transport materials in a straight line, they can be used to transport objects that are damaged, such as mechanical equipment in a factory, or to avoid damage to passageways. It has the disadvantage that it cannot be transported three-dimensionally and freely by bending.

固形物を管でもつて液体と一緒に搬送するとに
よつて、前記の欠点は解決される。この用途に、
例えば中心から外側に向かつて螺旋状の通路を有
するインペラを回転させるブレードレスインペラ
を有するの固形物ポンプが使用され、この種のポ
ンプが実際に魚移送ポンプとして利用されてい
る。
By transporting the solids together with the liquid in tubes, the above-mentioned disadvantages are overcome. For this purpose,
For example, a solids pump having a bladeless impeller rotating an impeller having a spiral passage from the center outward is used, and this type of pump is actually used as a fish transfer pump.

しかしこの構造のポンプは、回転するインペラ
で液体を加速する為、ポンプを通過するときに固
形物に多かれ少なかれ傷付きを生ずる。特にイン
ペラが空転してインペラ内に固形物が一時的に止
まると固形物の損傷は激増する。よつてこの種の
ポンプは、いかなる種類の固形物をも搬送できる
のでは決してなく、限られた傷付き難いあるいは
多少傷付いてもよい物の搬送にしか使用されな
い。
However, since a pump with this structure accelerates the liquid with a rotating impeller, the solid material is more or less damaged when it passes through the pump. In particular, if the impeller spins idly and solid objects temporarily stop inside the impeller, damage to the solid objects increases dramatically. Pumps of this type are therefore in no way capable of conveying solid objects of any kind, but are only used for conveying a limited number of non-perishable or somewhat perishable materials.

本発明者は、密閉構造の水槽を設け、この水槽
をセパレータよりも高所に配設し、水槽から水と
魚とを流下させる装置を開発した。(特開昭51−
63292号公報) この装置は、第5図に示すように、密閉構造の
水槽19に送風機20を連結し、送風機20で水
槽19内の空気を排気し、水槽19を大気圧以下
に減圧し、多量の空気を吸入させて魚を空気搬送
している。水槽19の送出側は循環ポンプ21か
ら補給される水で閉塞され、吸入空気は吸入ホー
ス22を通つて吸入され、この吸入空気によつて
魚体が空気と共に吸入される。
The present inventor has developed a device that provides a water tank with a closed structure, arranges this tank at a higher location than a separator, and allows water and fish to flow down from the tank. (Unexamined Japanese Patent Publication No. 1973-
Publication No. 63292) As shown in FIG. 5, this device connects a blower 20 to a water tank 19 with a closed structure, exhausts the air in the water tank 19 with the blower 20, reduces the pressure of the water tank 19 to below atmospheric pressure, The fish are transported by air by inhaling a large amount of air. The delivery side of the water tank 19 is closed with water supplied from the circulation pump 21, and intake air is sucked in through the suction hose 22, and the fish body is sucked together with the air by this intake air.

又、特開昭53−75094号公報並びに実開昭35−
32571号公報には、エアーリフトポンプを使用し
た揚魚装置が示されている。これ等の装置は、揚
魚管の下端に、空気、又は液体と空気の混合体を
吸き込み、揚魚管内の液体の見かけ比重を小さく
して液体と一緒に魚を吸い上げて移送している。
Also, Japanese Unexamined Patent Publication No. 1983-75094 and Utility Model Publication No. 1983-
Publication No. 32571 discloses a fish lifting device using an air lift pump. These devices suck air or a mixture of liquid and air into the lower end of the fish lifting tube, reduce the apparent specific gravity of the liquid in the fish lifting tube, and suck up and transport the fish along with the liquid. There is.

C 従来の問題点 第5図に示す構造の装置は、魚を高速空気流で
もつて空気移送しているが、空気移送は、液体移
送に比べると、搬送媒体が高速となる為、移送途
中に魚等の固形物が移送管の内面に衝突して損傷
が多くなる欠点を免れない。
C. Conventional Problems The device with the structure shown in Figure 5 pneumatically transports fish using a high-speed air flow, but in pneumatic transport, the conveyance medium is faster than in liquid transport, so This method inevitably suffers from the drawback that solid objects such as fish collide with the inner surface of the transfer pipe, causing more damage.

又、この装置のように、空気移送で魚を高所に
吸い上げ、その後液体と共に移送する装置は、密
閉構造の水槽内圧が大気圧以下に減圧され、しか
もこの圧力が、水槽に送りこまれる魚の送り込み
状態によつて大幅に変動する。従つて、水槽を相
当に高所に配設しても、水槽から勢いよく水が流
下せず、しかも、水槽圧力で水の流下量が変動す
る欠点があつた。
In addition, with a device like this device, which uses air to suck up fish to a high location and then transfer them along with the liquid, the internal pressure of the sealed aquarium is reduced to below atmospheric pressure, and this pressure is used to transport the fish into the aquarium. It varies greatly depending on the condition. Therefore, even if the water tank is placed at a fairly high location, the water does not flow down from the tank with great force, and furthermore, the amount of water flowing down varies depending on the tank pressure.

この為、水槽を相当に高所に配設する必要があ
つて簡単に設置できず、又高所の水槽の圧力がほ
ぼ大気圧に保持される状態にあつては、魚が勢い
よく流下されるが、この状態で移送管に固形物が
詰まると、固形物に無理な水圧が掛かつて弱る欠
点があつた。
For this reason, it is necessary to place the aquarium at a considerable height, which makes it difficult to install it easily, and when the pressure of the aquarium at a high place is maintained at approximately atmospheric pressure, the fish may be washed down with great force. However, if the transfer pipe becomes clogged with solid matter in this state, it has the disadvantage that unreasonable water pressure is applied to the solid matter, causing it to weaken.

今仮に、水槽内の圧力が大気圧よりも0.3気圧
低く減圧されるとすれば、水槽の水面レベルは
3m以上高所に配設しなければ移送されず、これ
を相当に高い位置に設置する必要がある。
Now, if the pressure inside the aquarium is reduced to 0.3 atm below atmospheric pressure, the water level in the aquarium will be
It cannot be transferred unless it is installed at a height of 3 meters or more, and it is necessary to install it at a considerably high position.

又、揚魚管の下端に空気を吹き込んで揚魚する
エアーリフトポンプは、魚が高速回転するインペ
ラ内を通過せず、しかも液体を搬送媒体として、
魚を移送する為、移送時に受ける魚の損傷は減少
できるが、動作原理から、使用状態に若しく制約
を受ける欠点がある。即ち、エアーリフトポンプ
は、揚魚管内に吹き込まれた空気によつて、揚魚
管内の液体の見かけ比重を小さくし、揚魚管下端
の水圧によつて液体が吸入されるので、揚魚管下
端の水深が浅い場合に効率が悪く、揚程以上では
全く移送不能となる欠点があり、水面下の比較的
深い位置から、水面上低い位置に揚魚する用途に
しか使用出来ない。
In addition, air lift pumps, which blow air into the lower end of the fish lifting tube to lift fish, do not allow the fish to pass through the impeller, which rotates at high speed, and use liquid as the transport medium.
Since the fish are transported, damage to the fish during transport can be reduced, but due to the principle of operation, there is a drawback that the conditions of use are limited. In other words, the air lift pump reduces the apparent specific gravity of the liquid in the fish lifting tube by using air blown into the fish lifting tube, and the liquid is sucked in by the water pressure at the lower end of the fish lifting tube. It has the disadvantage that it is inefficient when the water depth at the lower end is shallow, and cannot be transported at all above the lifting height, so it can only be used for lifting fish from a relatively deep position below the water surface to a low position above the water surface.

本発明は、従来の欠点を除去すること、即ち、
固形物が工場内の障害や人車の通路を避けて立体
移送できることに加えて、ミキシング部材を比較
的低い位置に配設でき、しかも、固形物がミキシ
ング部材からセパレータに向かつて無理な力を受
けることなく極めてスムーズに移送され、傷付き
易い固形物が傷付き少なく移送されるエアーポン
プ式固形物移送装置を提供することにある。
The present invention obviates the drawbacks of the prior art, namely:
In addition to being able to transport solids three-dimensionally while avoiding obstacles in the factory and passageways of passenger cars, the mixing member can be placed at a relatively low position, and solids can be moved from the mixing member to the separator without excessive force. To provide an air pump type solid matter transfer device which can transport easily-damaged solid matter extremely smoothly without being damaged, and can transport easily-damaged solid matter with less damage.

更に、本発明の他の重要な目的は、ミキシング
部材とセパレータの配設位置にほとんど制約を浮
けず、多用途に能率よく使用できるエアーポンプ
式固形物移送装置を提供することにある。
Furthermore, another important object of the present invention is to provide an air pump type solids transfer device that can be efficiently used for a variety of purposes, with almost no restrictions placed on the placement positions of the mixing member and the separator.

D 目的を達成する為の手段 第1図に示すエアーポンプ式固形物移送装置
は、固形物と液体とが溜められるミキシング部材
2と、このミキシング部材2から、固形物と液体
を移送する移送管4と、移送管4の先端に連結さ
れた固形物と液体とを分離するセパレータ3と、
移送管4内に空気を噴射する空気吹出部材5と、
移送管4内の空気を排気する真空ポンプ11とを
備える。
D Means for Achieving the Purpose The air pump type solids transfer device shown in Fig. 1 includes a mixing member 2 in which solids and liquid are stored, and a transfer pipe for transferring the solids and liquid from this mixing member 2. 4, a separator 3 connected to the tip of the transfer pipe 4 for separating solids and liquid,
an air blowing member 5 that injects air into the transfer pipe 4;
A vacuum pump 11 is provided to exhaust the air in the transfer pipe 4.

移送管4は、吸入端と吐出端との間に、立上部
4aと降下部4bとを有すべく中間で折曲されて
おり、立上部4aが吸入側となつてこれがミキシ
ング部材2の水面下に、降下部4bが吐出側とな
つてこれがセパレータ3に連通されており、立上
部4aの下部に空気吹出部材5が配設され、立上
部4aと降下部4bの中間で移送管の上端に真空
ポンプ11の吸入側が連結されている。
The transfer pipe 4 is bent in the middle to have a rising part 4a and a descending part 4b between the suction end and the discharge end, and the rising part 4a is the suction side and this is the water surface of the mixing member 2. Below, the descending part 4b becomes the discharge side and is communicated with the separator 3. An air blowing member 5 is disposed at the lower part of the rising part 4a, and the upper end of the transfer pipe is located between the rising part 4a and the descending part 4b. The suction side of the vacuum pump 11 is connected to the suction side of the vacuum pump 11.

E 作用、効果 本発明のエアーポンプ式固形物移送装置は、中
間で折曲されて液体が吸い上げられる立上部と、
液体が流下する降下部とからなる移送管を有し、
移送管の立上部は下部に噴射されて管内を浮上す
る空気でもつて見かけ比重が小さくなり、立上部
の比重差によつて液体が移送され、これによつて
魚がスムーズに移送される。即ち、液体移送のエ
ネルギは、立上部と降下部との圧力差によつて決
定され、両者の圧力差を一定範囲内に保持するか
ぎり、液体はほぼ同一の流速で移送される。この
ことは、固形物を常時理想的な移送速度で液体移
送できることになり、又、万一固形物が移送管の
途中に詰まつた場合でも、固形物に無理な力をか
けてこれを傷めることがなく、固形物移送時の傷
付きを極減して理想的な移送特性を実現する。
E Functions and Effects The air pump type solids transfer device of the present invention has a rising part that is bent in the middle and sucks up liquid;
It has a transfer pipe consisting of a descending part through which the liquid flows,
The apparent specific gravity of the rising part of the transfer pipe is reduced by the air that is injected into the lower part and floats inside the pipe, and the liquid is transferred due to the difference in specific gravity of the rising part, thereby allowing the fish to be transferred smoothly. That is, the energy for liquid transfer is determined by the pressure difference between the rising part and the falling part, and as long as the pressure difference between the two is kept within a certain range, the liquid is transferred at approximately the same flow rate. This means that solids can always be transferred to the liquid at an ideal transfer speed, and even if solids become clogged in the middle of the transfer pipe, there is no need to apply excessive force to the solids and damage them. It minimizes damage during solid material transfer and achieves ideal transfer characteristics.

更に、立上部と降下部との圧力差、正確には立
上部内の液体の見かけ比重×高さと、降下部内の
液体の比重×高さの差によつて液体と固形物とを
移送する為、従来のエアーリフトポンプでは能率
が悪くて使用できない状態、即ち、空気吹き出し
位置がミキシング部材の水面から浅く、又この水
深に比べてセパレータが高所に位置する場合でも
能率よく固形物を無損傷移送できる。
Furthermore, liquid and solid matter are transferred due to the pressure difference between the rising part and the falling part, more precisely, the difference between the apparent specific gravity of the liquid in the rising part x height and the specific gravity of the liquid in the falling part x height. , Even when conventional air lift pumps are inefficient and cannot be used, i.e., the air blowing position is shallow from the water surface of the mixing member, and the separator is located at a high place compared to this water depth, it can efficiently remove solids without damaging them. Can be transported.

又、移送管を立ち上げた後降下させるので、移
送管の一部にエアーリフトポンプを有するにもか
かわらず、ミキシング部材とセパレータとが同一
レベルの状態、即ち、揚程零の状態でも勿論能率
よく移送可能である。
In addition, since the transfer pipe is raised and then lowered, even though the transfer pipe has an air lift pump in a part of it, it is of course efficient even when the mixing member and the separator are at the same level, that is, when the head is zero. Transportable.

この為、ミキシング部材とセパレータとの設置
位置に制約を浮けず、使用現場に最適な位置にミ
キシング部材とセパレータとを配設して便利でし
かも能率よく固形物が移送できる特長が実現され
る。
For this reason, there are no restrictions on the installation positions of the mixing member and separator, and the mixing member and separator can be placed in the optimal position for the site of use, thereby realizing the advantage that solids can be transferred conveniently and efficiently.

又、ミキシング部材からセパレータへは、固形
物と液体とが管を介して移送される為、ミキシン
グ部材とセパレータとの間の移送間の配設位置に
制約を受けない、即ち、ミキシング部材とセパレ
ータとの途中に邪魔物があつても、これをさけて
配管できる。
Furthermore, since the solids and liquid are transferred from the mixing member to the separator via the pipe, there are no restrictions on the placement position between the mixing member and the separator. Even if there is an obstruction on the way to the pipe, the piping can be routed to avoid it.

この為、工場等に於て、壁等の障害物を避け、
あるいは人や車の通路を避け、あるいは又無駄な
スペースを利用して便利に移送できる。
For this reason, in factories etc., avoid obstacles such as walls,
Alternatively, it can be conveniently transported by avoiding the passage of people or cars, or by utilizing wasted space.

更に又、本発明の装置は、移送管の立上部の下
部に空気が吹き込まれ、これが立上部を浮上して
上部から真空ポンプで排気され、これによつて立
上部と降下部とに圧力差を発生させ、この圧力差
によつて魚等の固形物を移送している。この方式
によると、固形物を空気移送する部分がなく、空
気移送による損傷を極減して、全移送路における
固形物の損傷を少なくできる。
Furthermore, in the device of the present invention, air is blown into the lower part of the rising part of the transfer pipe, floats up the rising part, and is evacuated from the upper part by a vacuum pump, thereby creating a pressure difference between the rising part and the falling part. This pressure difference is used to transport solid materials such as fish. According to this system, there is no part for pneumatically transporting the solids, and damage caused by pneumatic transport can be minimized, making it possible to reduce damage to the solids along the entire transfer path.

F 好ましい実施例 以下、本発明の実施例を図面に基づいて説明す
る。
F Preferred Embodiments Hereinafter, embodiments of the present invention will be described based on the drawings.

第1図に示す固形物の移送装置は、例えば卵、
陶磁器、合成樹脂製品、畜肉魚介類、果物、野
菜、芋類、海草類、皮革シート状物、ハム、ソー
セージ等の固形物を搬送するもので、前工程に連
結されたコンベア(図示せず)から、固形物が供
給されてくると共に、固形物の搬送体である水や
海水等の液体が所要量溜められる箱型に形成され
たミキシング部材2と、このミキシング部材2よ
りも上方に位置して配設され、かつ液体を介して
固形物が搬送されてくるセパレータ3と、このセ
パレータ3と前記ミキシング部材2とに両端が連
結され、吸入側開口端は常に液中に潜没してここ
から空気を吸入しないように、ミキシング部材2
の水面より下方に連結されており、それ自体は垂
直状の立上部4aと降下部4bとを有すべく中間
でU曲された移送管4と、この移送管4の立上部
4aの下部に配設され、移送管の立上部4aに空
気を吹き込む空気吹出部材5と、移送管4の上端
に連結された真空ポンプ11とを備えている。
The solid material transfer device shown in FIG.
It transports solid materials such as ceramics, synthetic resin products, meat, seafood, fruits, vegetables, potatoes, seaweed, leather sheets, ham, sausages, etc., from a conveyor (not shown) connected to the previous process. , a box-shaped mixing member 2 in which the solids are supplied and a required amount of liquid such as water or seawater, which is a carrier for the solids, is stored; and a mixing member 2 located above the mixing member 2. A separator 3 is provided and to which solids are conveyed through the liquid, and both ends are connected to this separator 3 and the mixing member 2, and the opening end on the suction side is always submerged in the liquid and from there. Mixing member 2 to avoid inhaling air.
The transfer pipe 4 is connected below the water surface and is U-bent in the middle to have a vertical rising part 4a and a descending part 4b, and a lower part of the rising part 4a of the transfer pipe 4. It includes an air blowing member 5 which is arranged and blows air into the upright portion 4a of the transfer pipe, and a vacuum pump 11 connected to the upper end of the transfer pipe 4.

ミキシング部材2は移送管4内に固形物がスム
ーズに吸入されるように、移送される固形物の比
重が液体の比重より大きくて底に沈む場合、ミキ
シング部材2の底に、移送管4の吸入開口端を連
結し、さらに、ミキシング部材2の底面羅を、移
送間4の連結箇所に向かつて下り勾配に傾斜する
のがよい。
The mixing member 2 is provided at the bottom of the mixing member 2 so that the solids are sucked into the transfer pipe 4 smoothly. It is preferable that the suction opening ends are connected, and that the bottom surface of the mixing member 2 is also inclined downwardly toward the connection point of the transfer gap 4.

ミキシング部材2内の液体は移送管4によつ
て、セパレータ3に送られるので、セパレータ3
がセパレータタンク3aを備える場合、セパレー
タタンク3aの液体をミキシング部材2に戻すの
がよい。これを実現するには、ミキシング部材2
とセパレータタンク3aとに還水管6を連結し、
セパレータタンク3aの液体を還水管6によつて
ミキシング部材2に自然流入させればよい。
Since the liquid in the mixing member 2 is sent to the separator 3 through the transfer pipe 4, the separator 3
When the apparatus includes a separator tank 3a, it is preferable to return the liquid in the separator tank 3a to the mixing member 2. To achieve this, the mixing member 2
and a separator tank 3a with a water return pipe 6 connected to the separator tank 3a.
The liquid in the separator tank 3a may naturally flow into the mixing member 2 through the return pipe 6.

ところが、第1図に示すように、ミキシング部
材2とセパレータタンクB3aとの水面レベルが
ほぼ同一である場合、還水管6にポンプ7を連結
し、ポンプ7でもつてセパレータタンク3aの液
体をミキシング部材2に強制返還する。
However, as shown in FIG. 1, when the water levels of the mixing member 2 and the separator tank B3a are almost the same, a pump 7 is connected to the water return pipe 6, and the pump 7 also transfers the liquid in the separator tank 3a to the mixing member. 2 will be forcibly returned.

本発明は、固形物を、送り込まれてくる位置よ
りも高く移送することがほとんどであるので、通
常セパレータ3はミキシング部材2より高所、正
確には、セパレータ3の、移送管で固形物が送り
こまれる箇所がミキシング部材2よりも高所に配
設される。
In the present invention, in most cases, the solids are transferred higher than the position from which they are fed, so the separator 3 is usually placed higher than the mixing member 2, or more precisely, the solids are transferred to the transfer pipe of the separator 3. The part where the mixing member 2 is fed is arranged higher than the mixing member 2.

セパレータ3は上方に固形物の分離部材を備
え、分離部材は液体を通すが搬送される固形物を
通さない通水性を有する。
The separator 3 is provided with a solid separation member on the upper side, and the separation member has water permeability that allows the liquid to pass through but not the solids to be transported.

第1図の分離部材は傾斜して配設された多孔板
9で液体から分離された固形物は下方に滑り落と
される。
In the separating member shown in FIG. 1, the solid matter separated from the liquid is slid downward by the perforated plate 9 arranged at an angle.

第1図の移送管4はセパレータ3よりも上方に
延長され、ミキシング部材2に連結された吸入側
の下端に空気吹出部材5が連結され、上端に気水
分離して空気のみを回収する為のエアーセパレー
タ13が連結され、エアーセパレータ13の空気
吸出孔10は、真空ポンプ11の吸入側に連結さ
れて分離された空気を吸出する。
The transfer pipe 4 in FIG. 1 extends above the separator 3, has an air blowing member 5 connected to its lower end on the suction side connected to the mixing member 2, and has an air blowing member 5 connected to its upper end to separate air and water and collect only air. An air separator 13 is connected thereto, and an air suction hole 10 of the air separator 13 is connected to the suction side of a vacuum pump 11 to suck out the separated air.

空気吹出部材5は立上部4aの下端に連結さ
れ、立上部4aの下端に空気を送り込む。吹き込
まれた空気は、立上部を上昇して上端まで行つた
所で、エアーセパレータ13で水と分離され、空
気吸出孔10から吸い出される。
The air blowing member 5 is connected to the lower end of the upright part 4a, and blows air into the lower end of the upright part 4a. The blown air rises up the rising part and reaches the upper end, where it is separated from water by the air separator 13 and sucked out from the air suction hole 10.

移送管内に吹き出された空気は、液中で気泡状
となり、液体の見かけ比重を小さくする。ところ
で、気泡が大きいと、移送管内の水を撹拌して固
形物を傷めるので、気泡を小さくして液体と一緒
に上昇させるのがよい。これを実現するには、第
1図に示すように、空気吹出孔を、例えば微細な
連続気泡を有する合成樹脂発泡体や、粒状の金属
を通気性がある状態で焼結した金属等の微細気泡
発生部材12で覆うのがよい。
The air blown into the transfer pipe becomes bubbles in the liquid, reducing the apparent specific gravity of the liquid. By the way, if the bubbles are large, they will agitate the water in the transfer pipe and damage the solids, so it is better to make the bubbles small and allow them to rise together with the liquid. To achieve this, as shown in Figure 1, the air outlet holes must be made of a material such as a synthetic resin foam with fine open cells or a metal made by sintering granular metal in an air-permeable state. It is preferable to cover it with a bubble generating member 12.

本発明は、空気吹出部材5を移送管4内に空気
のみを吹き込むのに限定せず、空気と水との混合
体を吹き込むもの、および加圧水を吹き込んで高
速水流によつて空気を吸入するものを含む。
The present invention does not limit the air blowing member 5 to blowing only air into the transfer pipe 4, but also to blowing a mixture of air and water, and to blowing pressurized water to suck air with a high-speed water flow. including.

第2図および第3図は、移送管4の下部に空気
と水との混合体を上方に向けて吹き出す。空気と
水との混合体は、第3図に示すように、逆止弁1
4を介して、空気を吸入する空気孔15が開口さ
れた空気吸入管16と、この空気吸入管16内
に、軸方向に加圧水を噴射する加圧水ノズル17
とを備え、加圧水ノズル17から水を噴射するこ
とによつて、空気孔15から外気を吸入して、水
と空気の混合体を移送管4の下部に供給する。
2 and 3, a mixture of air and water is blown upward into the lower part of the transfer pipe 4. The mixture of air and water is transferred to the check valve 1 as shown in FIG.
4, an air suction pipe 16 with an air hole 15 for sucking air, and a pressurized water nozzle 17 that injects pressurized water in the axial direction into the air suction pipe 16.
By injecting water from the pressurized water nozzle 17, outside air is taken in from the air hole 15, and a mixture of water and air is supplied to the lower part of the transfer pipe 4.

第2図は、空気と水との混合体を、移送管4の
管壁を貫通するエジエクタノズル18から上方に
向けて噴射するもので、この場合、空気のみをエ
ジエクタノズル18から噴射することも可能であ
る。
In FIG. 2, a mixture of air and water is injected upward from an ejector nozzle 18 that penetrates the pipe wall of the transfer pipe 4. In this case, it is also possible to inject only air from the ejector nozzle 18. be.

第4図は、移送管4の下部に空気吸入管16が
連結され、空気吸入管16は、逆止弁14介在の
空気孔15で外気に開口され、かつ下から上に向
かつて高圧水を噴射する加圧水ノズル17を備
え、加圧水ノズル17から加圧水を噴射すること
によつて、高速水流でもつて空気孔15から外気
を吸入し、空気を移送管4内に供給する。
In FIG. 4, an air suction pipe 16 is connected to the lower part of the transfer pipe 4, and the air suction pipe 16 is opened to the outside air through an air hole 15 interposed in a check valve 14, and is directed from the bottom to the top to supply high-pressure water. A pressurized water nozzle 17 is provided, and by ejecting pressurized water from the pressurized water nozzle 17, outside air is sucked in from the air hole 15 with a high-speed water flow and the air is supplied into the transfer pipe 4.

本発明は、移送管の立上部の下部に空気吹出部
材を設けるが、本明細書に於て立上部の下部は特
に広い意味に使用するものとし、移送管内に空気
を吹き込んでポンプ作用を生ずる箇所を移送管の
下部とする。
In the present invention, an air blowing member is provided at the lower part of the upright part of the transfer pipe, but in this specification, the lower part of the upright part is used in a particularly broad sense, and air is blown into the transfer pipe to produce a pumping effect. The location is the bottom of the transfer pipe.

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

第1図は本発明の実施例を示すエアーポンプ式
固形物移送装置の断面図、第2図ないし第4図は
他の実施例を示す移送管の下部断面図、第5図は
従来の固形物移送装置の概略断面図である。 2……ミキシング部材、3……セパレータ、4
……移送管、5……空気吹出部材、6……還水
管、7……ポンプ、8……ネツトコンベア、9…
…多孔板、10……空気吸出孔、11……真空ポ
ンプ、12……微細気泡発生部材、13……エア
ーセパレータ、14……逆止弁、15……空気
孔、16……空気吸入管、17……加圧吸ノズ
ル、18……エジエクタノズル、19……水槽、
20……送風機、21……循環ポンプ、22……
吸入ホース。
FIG. 1 is a cross-sectional view of an air pump type solid material transfer device showing an embodiment of the present invention, FIGS. 2 to 4 are lower sectional views of a transfer pipe showing other embodiments, and FIG. 5 is a conventional solid material transfer device. It is a schematic sectional view of an article transfer device. 2...Mixing member, 3...Separator, 4
...Transfer pipe, 5...Air blowing member, 6...Return pipe, 7...Pump, 8...Net conveyor, 9...
... Porous plate, 10 ... Air suction hole, 11 ... Vacuum pump, 12 ... Fine bubble generating member, 13 ... Air separator, 14 ... Check valve, 15 ... Air hole, 16 ... Air suction pipe , 17... Pressure suction nozzle, 18... Ejector nozzle, 19... Water tank,
20...Blower, 21...Circulation pump, 22...
suction hose.

Claims (1)

【特許請求の範囲】 1 固形物と搬送媒体である液体が混合されるミ
キシング部材と、このミキシング部材から離され
て配設され、かつ送られてくる液体と固形物とを
分離するセパレータと、このセパレータと前記ミ
キシング部材とに両端著が連結され、吸入側はミ
キシング部材の水面レベルより下方に連結され、
かつそれ自体は吸入端と吐出端との間が立上部と
降下部とを有すべく中間で折曲され、立上部が吸
入側に、降下部が吐出側になつて、立上部がミキ
シング部材に、降下部がセパレータに連通される
移送管と、この移送管の立上部の下部に取り付け
られて、移送管の立上部に空気を吹き込む空気吹
出部材と、移送管の上端に吸入側が連結された真
空ポンプとを備え、該空気吹出部材から吹き出さ
れる空気によつて、立上部内の液体の見かけ比重
を小さくし、立上部と降下部との圧力差によつて
ミキシング部材内の液体をセパレータに移送し、
液体を介して固形物をミキシング部材からセパレ
ータに搬送するように構成されたエアーポンプ式
固形物移送装置。 2 移送される固形物の比重よりも液体の比重が
小さく、ミキシング部材の底に移送管の吸入側開
口端が連結され、かつミキシング部材の底面は移
送管の連結箇所に向つて下り勾配に傾斜されてい
る特許請求の範囲第1項記載のエアーポンプ式固
形物移送装置。 3 セパレータがセパレータタンクを備え、ミキ
シング部材とセパレータタンクとが還水管を介し
て連結され、セパレータタンク内の液体が還水管
を通つてミキシング部材に流入される特許請求の
範囲第1項記載のエアーポンプ式固形物移送装
置。 4 セパレータは上方に固形物の分離部材を備え
分離部材は液体を通すが搬送される固形物を通さ
ない通水性を有する特許請求の範囲第1項記載の
エアーポンプ式固形物移送装置。 5 空気吹出部材は、吹出口が微細気泡発生部材
で塞がれ、この微細気泡発生部材は、無数の空気
通路を有する通気性材料である特許請求の範囲第
1項記載のエアーポンプ式固形物移送装置。 6 微細気泡発生部材が、連続気泡を有する発泡
体である特許請求の範囲第5項記載のエアーポン
プ式固形物移送装置。 7 空気吹出部材が、空気と水との混合体を水の
移送方向に吹き出す特許請求の範囲第1項記載の
エアーポンプ式固形物移送装置。 8 空気吹出部材が、逆止弁を介して空気を吸入
する空気口が開口された空気吸入管と、この空気
吸入管内に、軸方向に圧力水を噴射する加圧水ノ
ズルとを備え、この加圧水ノズルから加圧水を吹
き込んで空気管内に空気を吸入し、空気と水との
混合体を移送管内に吹き込む特許請求の範囲第7
項記載のエアーポンプ式固形物移送装置。 9 空気吹出部材が、移送管の下部に連結された
空気吸入管と、この空気吸入管内に加圧水を噴射
する加圧水ノズルとを備え、空気吸入管は逆止弁
を介して空気を吸入する空気孔が開口され、加圧
水ノズルは水の移送方向に水を噴射し、噴射され
る高速水流によつて空気孔から空気を吸入するよ
うに構成された特許請求の範囲第7項記載のエア
ーポンプ式固形物移送装置。
[Scope of Claims] 1. A mixing member in which a solid substance and a liquid as a transport medium are mixed; a separator that is disposed apart from the mixing member and separates the liquid and the solid substance that are sent; Both ends are connected to the separator and the mixing member, and the suction side is connected below the water level of the mixing member,
The device itself is bent in the middle between the suction end and the discharge end to have a rising part and a descending part, with the rising part being on the suction side, the falling part being on the discharge side, and the rising part being a mixing member. A transfer pipe whose descending part communicates with the separator, an air blowing member attached to the lower part of the rising part of the transfer pipe to blow air into the rising part of the transfer pipe, and a suction side connected to the upper end of the transfer pipe. The air blown out from the air blowing member reduces the apparent specific gravity of the liquid in the rising part, and the pressure difference between the rising part and the falling part reduces the liquid in the mixing member. Transfer to separator,
An air pump solids transfer device configured to transport solids from a mixing member to a separator via a liquid. 2. The specific gravity of the liquid is lower than the specific gravity of the solids to be transferred, the suction side opening end of the transfer pipe is connected to the bottom of the mixing member, and the bottom surface of the mixing member is sloped downward toward the connection point of the transfer pipe. An air pump type solids transfer device according to claim 1. 3. The air according to claim 1, wherein the separator includes a separator tank, the mixing member and the separator tank are connected via a return pipe, and the liquid in the separator tank flows into the mixing member through the return pipe. Pump-type solids transfer equipment. 4. The air pump type solids transfer device according to claim 1, wherein the separator has a solids separation member on the upper side, and the separation member has water permeability that allows liquid to pass through but not the solids to be transported. 5. The air pump type solid material according to claim 1, wherein the air blowing member has a blowing outlet blocked with a fine bubble generating member, and the fine bubble generating member is a breathable material having countless air passages. Transfer device. 6. The air pump type solid matter transfer device according to claim 5, wherein the microbubble generating member is a foam having open cells. 7. The air pump solids transfer device according to claim 1, wherein the air blowing member blows out a mixture of air and water in the water transfer direction. 8. The air blowing member includes an air suction pipe having an open air port for sucking air through a check valve, and a pressurized water nozzle that injects pressurized water in the axial direction within the air suction pipe, and the pressurized water nozzle Claim 7: Air is sucked into the air pipe by blowing pressurized water into the air pipe, and a mixture of air and water is blown into the transfer pipe.
The air pump type solids transfer device described in . 9. The air blowing member includes an air suction pipe connected to the lower part of the transfer pipe, and a pressurized water nozzle that sprays pressurized water into the air suction pipe, and the air suction pipe has an air hole that sucks air through a check valve. 8. The air pump type solid state air pump type solid state according to claim 7, wherein the pressurized water nozzle is configured to inject water in the water transfer direction, and draw air from the air hole by the injected high-speed water flow. Object transfer device.
JP8438677A 1977-07-12 1977-07-12 Air pump type solid matter transfer device Granted JPS5418591A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP8438677A JPS5418591A (en) 1977-07-12 1977-07-12 Air pump type solid matter transfer device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8438677A JPS5418591A (en) 1977-07-12 1977-07-12 Air pump type solid matter transfer device

Related Child Applications (1)

Application Number Title Priority Date Filing Date
JP14465384A Division JPS6093034A (en) 1984-07-11 1984-07-11 Solids transport device

Publications (2)

Publication Number Publication Date
JPS5418591A JPS5418591A (en) 1979-02-10
JPS6150848B2 true JPS6150848B2 (en) 1986-11-06

Family

ID=13829113

Family Applications (1)

Application Number Title Priority Date Filing Date
JP8438677A Granted JPS5418591A (en) 1977-07-12 1977-07-12 Air pump type solid matter transfer device

Country Status (1)

Country Link
JP (1) JPS5418591A (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5781025A (en) * 1980-11-10 1982-05-20 Mitsubishi Heavy Ind Ltd Air lifter for slurry conveyance pipe
JPS6448720A (en) * 1987-08-19 1989-02-23 Mitsui Shipbuilding Eng Fish lifting device

Also Published As

Publication number Publication date
JPS5418591A (en) 1979-02-10

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