JPS594524A - Solid material transfer device - Google Patents

Solid material transfer device

Info

Publication number
JPS594524A
JPS594524A JP57110243A JP11024382A JPS594524A JP S594524 A JPS594524 A JP S594524A JP 57110243 A JP57110243 A JP 57110243A JP 11024382 A JP11024382 A JP 11024382A JP S594524 A JPS594524 A JP S594524A
Authority
JP
Japan
Prior art keywords
pump
tank
solids
rotary
air
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.)
Granted
Application number
JP57110243A
Other languages
Japanese (ja)
Other versions
JPH0362610B2 (en
Inventor
Takeshi Hayashi
武 林
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to JP57110243A priority Critical patent/JPS594524A/en
Priority to IS2806A priority patent/IS1413B6/en
Priority to DK220783A priority patent/DK220783A/en
Priority to ES523568A priority patent/ES8404944A1/en
Priority to NO832324A priority patent/NO157777C/en
Publication of JPS594524A publication Critical patent/JPS594524A/en
Publication of JPH0362610B2 publication Critical patent/JPH0362610B2/ja
Granted legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B65CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
    • B65GTRANSPORT OR STORAGE DEVICES, e.g. CONVEYORS FOR LOADING OR TIPPING, SHOP CONVEYOR SYSTEMS OR PNEUMATIC TUBE CONVEYORS
    • B65G53/00Conveying materials in bulk through troughs, pipes or tubes by floating the materials or by flow of gas, liquid or foam
    • B65G53/30Conveying materials in bulk through pipes or tubes by liquid pressure

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • Air Transport Of Granular Materials (AREA)
  • Crystals, And After-Treatments Of Crystals (AREA)
  • Refuse Collection And Transfer (AREA)
  • Feeding Of Articles To Conveyors (AREA)

Abstract

PURPOSE:To reduce damages to be made on solid materials and provide higher transfer ability by connnecting a rotary solid material pump and a sealed-tank solid material pump in series in a transfer system suited for transferring fishes together with sea water. CONSTITUTION:When unloading fishes out of a fish tank 30, first an air pump 3 is operated with a four-way valve 2 positioned at the solid line, to reduce the pressure in a sealed tank 1 which is the main body of a sealed-tank solid material pump. At this stage, check valves 5 and 6 are opened and closed respectively to allow the fishes and water in the fish tank 30 to be sucked up into the tank 1, and also to be flown into a rotary solid material pump 20 from which the air is discharged through an exhaust pipe 34. Then, the pump 20 is operated when the level of the water surface in the tank 1 reachs the middle point, and the air pump 3 is stopped when the level reaches the upper limit level. The fishes and water being transferred by pressure through the pump 20 are led to a water filtering separator 24 where fishes are separated from sea water through a selector comb 27.

Description

【発明の詳細な説明】 本発明は、水や海水等の液体を搬送媒体として、固形物
を管路で移送する装置に関し、特に、魚や果形等の水産
物や農産物を移送する装置に関する。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a device for transporting solid materials through a pipe using a liquid such as water or seawater as a transport medium, and particularly relates to a device for transporting fish, fruit-shaped marine products, and agricultural products.

■ 先行技術 液体を搬送媒体として固形物を移送する装置は、魚の移
送に最も多用される。
■ PRIOR ART Devices for transferring solids using liquid as the carrier medium are most commonly used for the transfer of fish.

この種の装置には、現在密閉タンクに液体と固形物とを
一緒に吸入、排出して移送する密閉タンク式固形物ポン
プと、回転するインペラで固形物と液体とを送るロータ
リ一式固形物ポンプとがある。ロータリ一式固形物ポン
プはプレードレスインペラ内を魚体が通過するので、能
率は良いが、空気を吸入するとインペラが空転して移送
作用を停止する。この状態に於て、ポンプ内で魚体が長
い時間回転される為、極端に魚体が損傷する。
Currently, this type of equipment includes a closed tank type solids pump, which sucks in and discharges liquid and solids together into a closed tank, and transfers them, and a rotary integrated solids pump, which sends solids and liquid with a rotating impeller. There is. The rotary solids pump has good efficiency because the fish pass through the bladeless impeller, but when air is sucked in, the impeller spins and stops the transfer action. In this state, the fish body is rotated within the pump for a long time, causing extreme damage to the fish body.

従って、ロータリ一式固形物ポンプは、ふんだんに水が
あって、空気を吸入しない海中からの水揚げのみに使用
される。魚槽内の魚がロータリ一式固形物ポンプによっ
て陸揚げされるのは好ましくない。というのは、魚槽の
角氷が減少してくると、吸入口から空気が吸入される為
である。
Therefore, the rotary solids pump is used only for unloading from the sea where there is plenty of water and no air is sucked. It is undesirable for fish in a fish tank to be landed by a rotary solids pump. This is because when the ice cubes in the fish tank decrease, air is sucked in through the intake port.

更に、このロータリ一式固形物ポンプは、いかなる場合
にも空気を吸入しないように、海中の網の中に直接吊り
込んで使用される。しかしながら、網の中の魚を揚魚で
きる能力のロータリ一式固形物ポンプは、例えば口径が
1501jlfm度のものでも重量が約300Kg以上
もあって極めて重く、しかもこれが波のある洋1−で、
船1−のデツキクレーンで吊り下げて使用されるので使
用し鍾く、K相当に危険な作業となる。又、ロータリ一
式固形物ポンプが海中に吊り下げられて運転されても、
これが空気を全く吸入しないことは難しく、海1−の波
によって、あるいは網や魚群等の状態によっては一時的
に多少の空気を吸入し易い。史に困ったことに、比較的
少量の空気を吸入するだけでロータリ一式固形物ポンプ
はポンプ作用を停止して空転し、また、この状態では全
くポンプ作用をしなくなるのでロータ内に吸入された空
気がスムーズに排出されず、ロータ内の魚が著しく損傷
を受ける。
Furthermore, this rotary solids pump is used by being suspended directly into an underwater net so as not to inhale air under any circumstances. However, a rotary solids pump capable of lifting fish in a net, for example, even one with a diameter of 1501 JLFm, weighs about 300 kg or more and is extremely heavy, and moreover, it is difficult to use in the ocean with waves.
Since it is used by being suspended by the deck crane of the ship 1-, it is difficult to use it, and the work is quite dangerous. Furthermore, even if a rotary solids pump is operated suspended in the sea,
It is difficult for this to not inhale air at all, but it is easy for it to temporarily inhale some air due to ocean waves or depending on the condition of the net or school of fish. Unfortunately, a rotary complete solids pump stops pumping and runs idly when only a relatively small amount of air is sucked in, and since there is no pumping action at all in this state, the solids pump is sucked into the rotor. The air cannot be exhausted smoothly and the fish inside the rotor will be seriously damaged.

密閉タンク式固形物ポンプけ、インペラ内を魚体が通過
しないので、魚の損傷が少なく、又、空気が吸入されて
も魚体が損傷することはない。従って、空気を吸わせな
が5でも揚魚が可能である。
Since the fish body does not pass through the impeller of the closed tank type solids pump, there is little damage to the fish, and even if air is inhaled, the fish body will not be damaged. Therefore, it is possible to fry fish even if the fish is not allowed to breathe air.

しかしながら、密閉タンクが液体と固形物とを吸入する
ときには、液体の排出が停止され、又、吐出中には吸入
されないバッチ移送で、しかも空気を介して移送するの
で、能串が悪い。密閉タンクを2個用意して一万のタン
クの成人中に能万のタンクを吐出させ、連続に近い状態
で移送することのできる双胴の密閉タンク式固形物ポン
プも開発されている。
However, when the closed tank takes in the liquid and solids, the discharge of the liquid is stopped, and the liquid is transferred in batches without being sucked in during discharge, and moreover, the liquid is transferred via air, which is inefficient. A twin-barrel closed-tank solids pump has also been developed that has two closed tanks and is capable of discharging 10,000 tons of solids into the 10,000-tank tank and transferring the solids in a nearly continuous state.

しかしながら、この構造の密閉タンク式固形物ポンプは
大型となり、小型漁船に積成することは相当に困難であ
る。又、密閉タンク式固形物ポンプは、エネルギ効率の
悪い真空ポンプを使用して密閉タンク内に角氷を吸入し
、又真空ポンプの排圧を利用して圧縮空気を密閉タンク
内に圧入する構造の為、密閉タンク内の真空度がある程
度上昇しなけれは角氷は吸入されず、更に吐出行程の最
終には最も高デの圧縮空気をそのまま排出しなければな
らないので、当然エネルギ効率が悪くなる。
However, a closed tank solids pump with this structure is large, and it is quite difficult to store it on a small fishing boat. In addition, closed tank type solids pumps use an energy-inefficient vacuum pump to suck ice cubes into a closed tank, and use the vacuum pump's exhaust pressure to pressurize compressed air into the closed tank. Therefore, the ice cubes will not be sucked in unless the degree of vacuum within the sealed tank increases to a certain degree, and furthermore, at the end of the discharge stroke, the compressed air with the highest degree of depletion must be discharged as is, which naturally results in poor energy efficiency. .

又、ロータリ一式固形物ポンプは比較的大型魚の揚魚に
は適している。が、小型魚には必ずしも最適のポンプで
はない。それは、漁網中の活魚の場合でも、又魚槽中の
鮮魚(死魚)の場合でも魚体が大型となる程、サクショ
ンホース内の色水密度が低くなり、即ち魚体の密度が薄
くなるので、高速で回転するインペラ中を通過しても魚
体の損傷は少なく、又、大型魚種表面の安値も丈友であ
る。しかじ片口いわし等の小型魚は相当に網中でも密集
し、又、魚槽中の密集した状態のままサクションホース
に吸入されるので、色水密度の高い状態でインペラ中を
通過して、極端に魚体が損傷を受けるものである。
Also, the rotary solids pump is suitable for lifting relatively large fish. However, it is not necessarily the best pump for small fish. This is because, whether it is live fish in a fishing net or fresh fish (dead fish) in a fish tank, the larger the fish, the lower the density of the colored water in the suction hose, which means the density of the fish becomes thinner. There is little damage to the fish body even when it passes through the impeller rotating at high speed, and the low price on the surface of large fish species is also durable. Small fish such as Shikaji Katakuchi Sardines are quite dense in the net, and they are sucked into the suction hose in a dense state in the fish tank, so the colored water passes through the impeller in a highly dense state, causing extreme This causes damage to the fish body.

ロータリ一式固形物ポンプと密閉タンク式固形物ポンプ
は、前述のような独特の特性を備えるが、それぞれ用途
が著しく制限され、又、使用状態の変化に充分対応でき
ない。液体を移送媒体とする固形物移送装置は、コンベ
ア等の池の移送装置とは比較にならない捏難しい特性が
要求される。この特性とは、膨大な喰の角が極めて短詩
に移送され、しかもいかなる場合も魚の損傷が最小限に
阻市されなければならないことである。
Although the rotary complete solids pump and the closed tank solids pump have the above-mentioned unique characteristics, their respective applications are severely limited and they cannot adequately respond to changes in usage conditions. Solids transfer devices that use liquid as a transfer medium are required to have characteristics that are difficult to knead compared to pond transfer devices such as conveyors. This characteristic is that a huge amount of horn can be transported in a very short time, and in any case the fish must be stopped with minimal damage.

従来から使用されている密閉タンク式固形物ポンプとロ
ータリ一式固形物ポンプとはこの両特性を満足できない
。従って、密閉タンク式固形物ポンプとロータリ一式固
形物ポンプの用途は著しく制限されている。この為、網
で捕獲された魚は、現在に致るも、はとんど例外なく、
別の網で掬い1−げて揚魚されている。
The closed tank type solids pump and the rotary type solids pump that have been used conventionally cannot satisfy both of these characteristics. Therefore, the applications of closed tank solids pumps and rotary solids pumps are severely limited. For this reason, even today, almost all fish caught with nets are
The fish are scooped up using another net and then fried.

(2′)  目的 本発明は、液体を搬送媒体とする固形物移送装置が実現
できなかった特性、即ち、常に用途に最適の状態で使用
でき、時間当りの移送能力を太きくして固形物を傷付き
少なく移送できる固形物の移送装置を提供するにある。
(2') Purpose The present invention has characteristics that cannot be achieved by solid material transfer devices that use liquid as a transport medium, that is, it can always be used in the optimum state for the purpose, and has a large transport capacity per hour to transport solid materials. To provide a device for transferring solids that can be transferred with less damage.

更に、本発明の能の重要な目的は、密閉タンク内 ている為、密閉タンクに連結された減圧手段によってロ
ータリ一式固形物ポンプに流入する空気■を減少でき、
運転途中に於けるロータリ一式固形物ポンプの空転を減
少できる固形物の移送装置を提供するにある。
Furthermore, an important objective of the present invention is that since the pump is in a closed tank, air flowing into the rotary solids pump can be reduced by means of a pressure reduction means connected to the closed tank.
To provide a solids transfer device capable of reducing idling of a rotary solids pump during operation.

更に又、密閉タンク式固形物ポンプとロータリ一式固形
物ポンプとが直列に接続されている為、いずれか一方を
運転し、あるいは一時的に両ポンプを運転して固形物が
移送でき、更に、密閉タンク式固形物ポンプで固形物を
移送するときに固形物がロータリ一式固形物ポンプ内を
通過するが、この状態で固形物は傷付き少なく移送され
る固形物の移送装置を提供するにある。
Furthermore, since the closed tank type solids pump and the rotary solids pump are connected in series, solids can be transferred by operating either one or both pumps temporarily. To provide a solid material transfer device in which the solid material passes through a rotary solid material pump when the solid material is transferred by a closed tank type solid material pump, and the solid material is transferred with less damage in this state. .

(3)構成 以ド、本発明の実施例を図面に基づいて説明する。(3) Configuration Hereinafter, embodiments of the present invention will be described based on the drawings.

第1図に示す固形物移送装置は、密閉タンク式固形物ポ
ンプと、ロークリ一式固形物ポンプ20とを備えている
。密閉タンク式固形物ポンプとロータリ一式固形物ポン
プ20とはUいに直列に連結され、ロータリ一式固形物
ポンプの吸入側に密閉タンク式固形物ポンプの吐出(′
l111か連結されている。
The solids transfer device shown in FIG. 1 includes a closed tank type solids pump and a rotary type solids pump 20. The closed tank solids pump and the rotary solids pump 20 are connected in series, and the discharge side of the closed tank solids pump is connected to the suction side of the rotary solids pump 20.
l111 is connected.

密閉タンク代置彫物ポンプは、固形物混合の液体が貯え
られる気密に密閉された密閉タンク1と、この密閉タン
ク1に連通きれて、内部の空気を排出する減圧手段並ひ
に密閉タンク内に空気を供給する給気手段とを併用する
四方切換弁2及び空気ポンプ3と、密閉タンク1の通路
である吸入口4に連結された吸入弁である逆止弁5と、
密閉タンク1の吐出側に連通された排出弁である逆11
・弁6とを備えている。
The closed tank replacement carving pump has an airtight closed tank 1 in which liquid mixed with solids is stored, a decompression means that communicates with this closed tank 1, and discharges the air inside, and a pressure reduction means inside the closed tank. A four-way switching valve 2 and an air pump 3 that are used together with an air supply means for supplying air; a check valve 5 that is an intake valve connected to an intake port 4 that is a passage of the sealed tank 1;
A reverse 11 is a discharge valve connected to the discharge side of the sealed tank 1.
・Equipped with valve 6.

密閉タンク1は、ここに固形物混合の液体か、例えば0
.5m〜5 nr117能できる内審槓を有し通路と空
気]−18とが開[−1されている。通路は吸入114
と排出ロアとからなり、排出[17は密閉タンクの底部
に、密閉タンクの1−Fの中間に吸入N4か開口されて
おり、上部には、密閉タンク1内の空気を排出し、また
内部に空気を圧入する空気1’+ 8か開口されており
、更に、内部の液面レヘルを検出するレベルセンサ9を
備えている。
The closed tank 1 is filled with liquid mixed with solids, for example, 0
.. 5m~5nr117 It has an internal inspection tower that can be used and the passageway and air]-18 are open [-1]. Passage is intake 114
and a discharge lower, the discharge [17] is an opening at the bottom of the sealed tank, between 1-F of the closed tank, and the upper part is for discharging the air inside the closed tank 1, and for internal There is an opening for air 1'+8 to pressurize air into the tank, and a level sensor 9 for detecting the internal liquid level is also provided.

密閉タンク1は、全体あるいは底部か水゛11断面円形
となる円筒状に形成され、排1f!117は、第2図な
いし第5図に示す如く、密閉タンク1の底部に接線方向
に開1]される。
The closed tank 1 is formed into a cylindrical shape with a circular cross section either entirely or at the bottom. 117 is opened 1] in the tangential direction at the bottom of the closed tank 1, as shown in FIGS. 2 to 5.

この方向に開[Jされた排出[■17は、第2図に示す
如く、密閉タンク1内の液体かタンク内面に沿つて矢印
の方間に旋回しながら移動し、液中の固形物である魚体
は、比重が水よりも多少重いの゛でゆっくりと底に沈降
し、このとき@は密閉タンク1の壁面に治って整列され
、Ut出「17の開口部では排出[−17の長さ方向に
向けられてスムーズに排出される。
As shown in Fig. 2, the discharge [17] opened in this direction is caused by the liquid in the closed tank 1 moving along the inner surface of the tank in the direction of the arrow, and solids in the liquid. A certain fish body, whose specific gravity is somewhat heavier than water, slowly sinks to the bottom. It is turned in the opposite direction and is ejected smoothly.

排出[17に連通式れる排出管10は、第2図に示す如
く、液体の移送方向に向かって断面形状が方形状から円
形に変形されている。
As shown in FIG. 2, the discharge pipe 10 communicating with the discharge pipe 17 has a cross-sectional shape that is changed from a rectangular shape to a circular shape in the direction of liquid transfer.

密閉タンク1は、第3図に示すように、底部をド窄み円
垂状とするか、あるいは第4図に示す妬く、全体を円筒
状に形成する。下窄み円錐状に形成された密閉クンク1
は、底部に角が集合し易く、密閉タンク内のI+をより
スムーズに残らず送り出しできる特長かある。
The closed tank 1 has a concave bottom shape as shown in FIG. 3, or has a cylindrical shape as a whole as shown in FIG. 4. Sealed kunk 1 formed in a conical shape with a narrowing downwards
This has the advantage that the corners tend to gather at the bottom, allowing the I+ inside the sealed tank to be sent out more smoothly without leaving any residue.

密閉タンクの全体形状によらず、排出口は接線方向に向
けて開[Iされるのがよい。
Regardless of the overall shape of the closed tank, it is preferable that the outlet be opened in the tangential direction.

吸入[−14に連結される好ましい形状の流入ダクト1
1が第5図に示されている。この流入ダクト11は、上
方に向かって断面積が太きくなるようにその幅がしたい
に広く形成されており、I一端部が、第1図および第4
図に示すように、密閉タンク1に向けて水平方向に折曲
されている。この形状の流入ダクト11は、密閉タンク
1の吸入[14に近づくに従って液体の流通が遅くなる
ので、固形物をゆっくりとスムーズに密閉タンク1内に
案内できる。
Inflow duct 1 of preferred shape connected to suction [-14
1 is shown in FIG. The inflow duct 11 is formed as wide as possible so that the cross-sectional area increases upwardly, and one end I is formed as shown in FIGS. 1 and 4.
As shown in the figure, it is bent horizontally toward the closed tank 1. In the inlet duct 11 having this shape, the flow of liquid becomes slower as it approaches the intake [14] of the closed tank 1, so that solids can be guided slowly and smoothly into the closed tank 1.

密閉タンク1の水平断面積は、吸入114並びに排出[
)γの開[−1面積に比べて充分に大きい、この為、1
汲人[]4に連結されるザクジョンホース12を通って
、液体と一緒に気泡か吸入されたとしても、密閉タンク
1内に於けるド向きの流速は気泡の浮上油Iヶに比べて
遅く、気泡は密閉タンク11・部に浮1−シて空気口か
ら排出される。
The horizontal cross-sectional area of the closed tank 1 includes the suction 114 and the discharge [
) γ is sufficiently large compared to the area [-1, therefore, 1
Even if bubbles are inhaled together with the liquid through the Zakujo hose 12 connected to the pump 4, the flow velocity in the direction of the air in the closed tank 1 will be lower than that of the floating oil I of the bubbles. After a while, the air bubbles float in the closed tank 11 and are discharged from the air port.

空気[18は、密閉タンク1内に溜まる空気を排出する
ものであるから、密閉タンク1の上部に開11される。
Since the air [18 is for discharging the air accumulated in the closed tank 1, it is opened 11 at the top of the closed tank 1.

第1図に示される密閉タンクの空気口8は、密閉タンク
1内の空気を排出する排気口と、密閉タンク内に空気を
供給する給気[jとを兼用する。N[気(−1と給気[
1とを密閉タンクに別々に開[]する場合、排気[1に
は密閉タンク1−、部に開口しなければならないか、給
気[1は必ずしも密閉タンク1一部に開[lする必要は
ない。
The air port 8 of the closed tank shown in FIG. 1 serves both as an exhaust port for discharging the air inside the closed tank 1 and as an air supply [j] for supplying air into the closed tank. N [air (-1 and supply air [
If 1 and 1 are opened separately into a closed tank, the exhaust [1 must be opened to the closed tank 1-, or the supply air [1 must be opened to a part of the closed tank 1]. There isn't.

空気ポンプ3は、密閉タンク内から空気を排出するのと
、密閉タンク内に空気を圧入するのに兼用される。よっ
て、この空気ポンプ3は、第1図に示す如く、四方切換
弁2を介して、吸入側と吐出側とが密閉タンク1に連結
されている。
The air pump 3 is used both to discharge air from the closed tank and to pressurize air into the closed tank. Therefore, as shown in FIG. 1, the air pump 3 has its suction side and discharge side connected to the closed tank 1 via the four-way switching valve 2.

密閉タンク1内に空気を圧入するものは、ロータリ一式
固形物ポンプの運転を停止した状態で、密閉タンク1内
の液を加圧して遠方に、あるいは高所に移送できる。た
た密閉タンク1内の液体を密閉タンクの近傍でそのトガ
に移送する場合、図示しないが、密閉タンクの給気手段
は、密閉タンクの上部をり1気に開放する給気弁たけで
充分である。給気弁は、密閉タンクの上部に連結され、
これが開角すると、密閉タンク内に大気が流入し、これ
によって密閉タンク内の液体か流出する。
The device that pressurizes air into the sealed tank 1 can pressurize the liquid in the sealed tank 1 and transfer it to a distant place or a high place while the rotary solids pump is stopped. When the liquid in the closed tank 1 is transferred to the toga near the closed tank, an air supply valve that opens the top of the closed tank at once is sufficient as an air supply means for the closed tank, although not shown. It is. The air supply valve is connected to the top of the closed tank,
When this angle opens, air flows into the closed tank, causing the liquid inside the tank to flow out.

レヘルセンザ9は、34.の?Ii極俸13を備えてオ
リ、各電極体13a、13b、13cは密閉タンク1の
中心に垂直に配設されている。この位置に配設された電
極体13は、密閉タンク1内を旋同する液体の中心にあ
って流速による力がほとんと作用しない。
Rehersenza 9 is 34. of? The electrode bodies 13a, 13b, and 13c are arranged vertically in the center of the closed tank 1. The electrode body 13 disposed at this position is located at the center of the liquid swirling inside the closed tank 1, and is hardly affected by force due to the flow velocity.

空気ポンプ3I/′i、密閉タンク1内に液体が1吸入
されるに充分な真空度にできる真空ポンプ、例えば1段
ないし多段の液封真空ポンプやルーツ真空ポンプが使用
される。
The air pump 3I/'i is a vacuum pump capable of creating a degree of vacuum sufficient to suck one liquid into the closed tank 1, such as a one-stage or multi-stage liquid ring vacuum pump or a Roots vacuum pump.

図示しないが、空気ポンプに、反転することによって吸
入側と吐出側とか反転して空気の移送方向か逆転する空
気ポンプ、例えばルーツポンプや液封式真空ポンプを使
用する場合、四方gJ換弁は必ずしも必要でなく、空気
ポンプの吸入側か吐出側のいずれか一刀を密閉タンクに
連結し、モータ等の動力源を反転して、真空ポンプと加
圧ポンプとに併用する。
Although not shown, when using an air pump that can be reversed to transfer the air between the suction side and the discharge side, or reverse the direction of air transfer by reversing the direction, such as a Roots pump or a liquid ring vacuum pump, a four-way gJ switching valve is not necessarily required. Although it is not necessary, connect either the suction side or the discharge side of the air pump to a closed tank, reverse the power source such as a motor, and use it as both a vacuum pump and a pressure pump.

密閉タンク1の吸入側と吐出()10に連結される逆I
I−弁5.6は、スイング動作の逆上弁が使用される。
An inverted I connected to the suction side of the sealed tank 1 and the discharge ( ) 10
The I-valve 5.6 is a swing-action reverse valve.

吸入側の逆上弁5は、サクションホース12から密閉タ
ンク1に向かって液体が流動するときにたけ開弁し、吐
出側の逆+It弁6は、密閉タンク1から液体か排出さ
れるときにだけ開弁する。
The reverse valve 5 on the suction side opens when liquid flows from the suction hose 12 toward the closed tank 1, and the reverse +It valve 6 on the discharge side opens when liquid is discharged from the closed tank 1. Only open the valve.

排出側の逆上弁6は、第1図に示すように、ロータリー
装置彫物ポンプ20の吐出側に連結するのがよい。この
イでl置に逆f1−弁6が連結された固形物移送装置は
、空気ポンプ3を運転して密閉タンク1内の空気を排出
するときに、密閉タンク内の空気と一緒にロータリ一式
固形物ポンプ20内の空気も排出される。よって、密閉
タンク1に液体が吸入された後は、ロータリ一式固形物
ポンプ20を運転後直ちにこれか液体の移送を開始する
The discharge side reverse valve 6 is preferably connected to the discharge side of a rotary carving pump 20, as shown in FIG. In this case, when the air pump 3 is operated to discharge the air in the sealed tank 1, the solids transfer device connected to the reverse f1-valve 6 at Air within the solids pump 20 is also exhausted. Therefore, after the liquid is sucked into the closed tank 1, the rotary solids pump 20 is operated and immediately starts transferring the liquid.

ロータリ一式固形物ポンプ20は、第1図又は第6図に
示す如く、好ましくは密閉タンク1のド方又は同レベル
に配設される。この位置にあるロータリ一式固形物ポン
プ20は、吸入[]19が密閉タンク1内の液面レベル
下にあって常に液体で満たされ、起動がスムーズで空転
を起こし難い。
As shown in FIG. 1 or FIG. 6, the rotary solids pump 20 is preferably disposed on the side of the closed tank 1 or at the same level. In the rotary solids pump 20 in this position, the suction [ ] 19 is below the liquid level in the closed tank 1 and is always filled with liquid, so that startup is smooth and idling is less likely to occur.

図示しないが、ロータリ一式固形物ポンプを密閉タンク
よりも1一方に配設することも可能である。
Although not shown, it is also possible to arrange the rotary solids pump on one side of the closed tank.

;CO場合、ロータリ一式固形物ポンプは、密閉タンク
内か加圧されて液体が圧入されるか、あるいは排気管で
吸入側の空気を排出して起動される。
; In the case of CO, the rotary solids pump is activated either by pressurizing the closed tank and injecting liquid, or by discharging the air on the suction side with an exhaust pipe.

密閉タンク1に連結された空気ポンプ3が、ロータリ一
式固形物ポンプ20内の空気をよりスムーズに排気する
には、ロータリー代置形輪ポンプ20の吸入管14側立
上部の一1―端に排気管34を連結し、この排気管3′
4を密閉タンク1の空気口8に連通ずる。のがよい。排
気管34が連結されるべく吸入管14に開[1された吸
気[115は、空気は通るが固形物は通過しない多孔板
16が張設されており、空気ポンプに魚のうろこや異物
等が吸入されるのを防上する。
In order for the air pump 3 connected to the sealed tank 1 to more smoothly exhaust the air inside the rotary solids pump 20, the air pump 3 connected to the sealed tank 1 should exhaust the air to one end of the upright part on the side of the suction pipe 14 of the rotary replacement type ring pump 20. A pipe 34 is connected to the exhaust pipe 3'.
4 is connected to the air port 8 of the sealed tank 1. It is better. A perforated plate 16 is installed in the intake pipe 115, which is opened to the intake pipe 14 to which the exhaust pipe 34 is connected, to allow air to pass through but not to allow solid matter to pass through. Prevents inhalation.

密閉タンク1に開[1される通路はひとつでもよい。ひ
とつの通路32は、第6図に示すように分岐管33で2
分岐され、分岐管の−・万に吸入弁である逆f1−弁5
が連結され、池の一部の分岐管が吸入@−14を介して
ロータリ一式固形物ポンプ20の吸入側に連結されてい
る。
The number of passages opened in the closed tank 1 may be one. One passage 32 is divided into two branch pipes 33 as shown in FIG.
The inverse f1-valve 5 is branched and is a suction valve in the branch pipe.
are connected, and a branch pipe of a part of the pond is connected to the suction side of the rotary solids pump 20 via the suction@-14.

ロータリ一式固形物ポンプ20は、回転するロータでも
って固形物混合の液体を移送するポンプで、第7図及び
第8図の断面図に示される如く、円形のケーシング17
内をロータ18が回転する。
The rotary solids pump 20 is a pump that transfers liquid mixed with solids using a rotating rotor, and as shown in the cross-sectional views of FIGS. 7 and 8, a circular casing 17 is used.
A rotor 18 rotates inside.

ケーシング17は片側の中心に吸入口119が開口され
、外周には、接線方向に向けて送出口21が開[1きれ
ている。
The casing 17 has an inlet 119 opened at the center of one side, and an outlet 21 opened in the tangential direction on the outer periphery.

ロータ18は、片側に回転軸22が固定され、回転軸2
2が軸受を介してケーシング17に支承され、ケーシン
グ17の吸入口1に対向する中心から外周に向かって渦
巻状の通過路23が穿設されたブレードレスのロータで
ある。このロータ18がモータ等で回転されると、通過
路23内の液体が遠心力によって加速され、送出口21
から圧送される。
The rotor 18 has a rotating shaft 22 fixed to one side, and the rotating shaft 22 is fixed to one side.
A bladeless rotor 2 is supported by a casing 17 via a bearing, and has a spiral passage 23 formed from the center of the casing 17 facing the suction port 1 toward the outer circumference. When this rotor 18 is rotated by a motor or the like, the liquid in the passageway 23 is accelerated by centrifugal force, and the liquid in the outlet 21
It is pumped from

ブレードレスのロータ18には、第9図と第10図に示
すように、2つの通過路23を有するものもあるが、本
発明の移送装置には、第6図及び第7図に示す単一の通
過路230ロータがよい。
Although some bladeless rotors 18 have two passageways 23 as shown in FIGS. 9 and 10, the transfer device of the present invention has a single passage 23 as shown in FIGS. 6 and 7. One passageway 230 rotor is preferable.

というのは、2通過路のロータ1Bは、バランスが取り
易く、又空気を吸入しても回転時の動バランスが崩れる
ことはないが、分岐部分で突出部ができる為、吸入され
た魚体がここに衝突して傷付き易く、K、長尺物を吸入
するとロータに巻き付いてスムーズに排出されない為で
ある。
This is because the rotor 1B, which has two passages, is easy to balance and does not lose its dynamic balance during rotation even if air is inhaled, but because a protrusion is formed at the branching part, the inhaled fish This is because they are easily damaged by collisions, and if a long object is sucked in, it will wrap around the rotor and not be ejected smoothly.

ただ屯−の通過路のロータ18は、通過路23内が液体
で満たされた状態で動バランスが取られている為、通過
路内に空気が吸入されると極端にバランスがくずれて軸
受等を傷め易い。従って、この形式の固形物ポンプは、
魚を傷めないことからも、またポンプに損傷を与えない
ことからも、空気の吸入は極力避けなければならない。
However, since the rotor 18 in the tunnel passageway is dynamically balanced with the passageway 23 filled with liquid, if air is sucked into the passageway, the balance will be extremely lost and the bearings etc. easy to damage. Therefore, this type of solids pump is
Inhalation of air must be avoided as much as possible to avoid damaging the fish and the pump.

第1図に於て、ロータリ一式kQ#物ポンプの送出[1
21は、逆上弁6を介して水切セパレータ24に連結さ
れる。水切セパレータ24は、液体を搬送媒体として移
送されて来た魚等の固形物を液体から分離するもので、
垂直状に)rてられて、水平ないし多少下向きに折曲さ
れた移送管25の先端に連結されている。
In Fig. 1, the rotary set kQ# material pump delivery [1
21 is connected to the drain separator 24 via the reverse valve 6. The drain separator 24 separates solids such as fish that have been transferred using the liquid as a transport medium from the liquid.
It is connected to the tip of a transfer pipe 25 which is bent vertically (vertically) and bent horizontally or slightly downward.

この水切セパレータ24Fi、液体が流−ドすべく傾斜
された液の受箱26と、この受箱26に斜設された選別
櫛27と、受箱26の下方に配設された溜槽28とから
なる。
This water draining separator 24Fi is composed of a liquid receiving box 26 which is inclined for liquid to flow, a sorting comb 27 provided obliquely to this receiving box 26, and a reservoir 28 disposed below the receiving box 26. Become.

選別櫛27は、少なくとも上面は、角の流下方向に平行
な格子状に形成されており、この]―に供給される固形
物を液体から分離する。
At least the upper surface of the sorting comb 27 is formed in the form of a grid parallel to the flow direction of the corners, and separates the solids supplied to this comb from the liquid.

溜槽28は、還水ホース29を介して、魚槽30に連結
され、移送されてきた液体の一部あるいは全部を魚槽3
0に還流する。
The reservoir tank 28 is connected to the fish tank 30 via a water return hose 29, and transfers some or all of the transferred liquid to the fish tank 3.
Reflux to 0.

第1図に示される固形物移送装置は極めて多種多様の用
途に使用できるが、その代表的な要途として、魚槽30
内の魚を陸揚げする場合の運転状態を例示すると、 111  まず四方ゾ換弁2を第1図の実線位置の状態
として空気ポンプ3を運転すれば、密閉タンク1内の空
気が空気ポンプ3によって排出され、密閉タンク1が減
圧される。この場合吐出側の逆+h弁6は閉面され、吸
入側の逆上弁5は開弁し、魚槽30中の角氷が密閉タン
ク1内へ吸揚げられ次第に角氷レベルが1〕昇する。第
1図の実施例知於てはロータリ一式固形物ポンプ20は
密閉タンク1より若11下方に位置するように据付けら
れているので、ロータリ一式固形物ポンプ20内部にも
魚JJ(が流入する。このとき、密閉タンク1とロータ
リ一式固形物ポンプ20とを連結する吸入管14の吸気
1’l 15に連結された排気管34からもロータリ一
式固形物ポンプ20内の空気が排出され、角氷はロータ
リ一式固形物ポンプ20に円滑に流入される。密閉タン
ク1内の液面レベルが中間水位検出レベルに達すれば、
このことが中間の長さを有する電極体13bに検出され
、レベルセンサ9の信号によってロータリ一式固形物ポ
ンプ2゜が運転される。この状態でサクションホース1
2内にあった若干の空気が密閉タンク1内へ流入しても
、空気ポンプ3も排列運転しているので密閉タンク1内
の空気は速やかに排出され、ロータリ一式固形物ポンプ
、20は正常な運転状態となる。
The solids transfer device shown in FIG.
To give an example of the operating conditions when landing fish in a tank, 111 First, if the air pump 3 is operated with the four-way switching valve 2 in the position shown by the solid line in Figure 1, the air in the closed tank 1 will be exhausted by the air pump 3. The closed tank 1 is depressurized. In this case, the reverse +h valve 6 on the discharge side is closed, and the reverse upward valve 5 on the suction side is opened, and the ice cubes in the fish tank 30 are sucked up into the sealed tank 1, and the ice cube level gradually rises to 1]. do. In the embodiment shown in FIG. 1, the rotary solids pump 20 is installed so as to be located below the closed tank 1, so that fish JJ( At this time, the air inside the rotary solids pump 20 is also exhausted from the exhaust pipe 34 connected to the intake air 1'l 15 of the suction pipe 14 connecting the sealed tank 1 and the rotary solids pump 20, and the air inside the rotary solids pump 20 is exhausted. The ice is smoothly flowed into the rotary solids pump 20. When the liquid level in the closed tank 1 reaches the intermediate water level detection level,
This is detected by the electrode body 13b having an intermediate length, and the rotary solids pump 2° is operated by the signal from the level sensor 9. In this state, suction hose 1
Even if some of the air that was in the tank 2 flows into the sealed tank 1, the air in the sealed tank 1 is quickly exhausted because the air pump 3 is also in parallel operation, and the rotary solids pump 20 is normal. It will be in a normal driving condition.

密閉タンク1内が、」−眼レベルに達すれば、このこと
が最も短かl/−1電極棒13cK検jISされ、レベ
ルセンサ9の出力される信号によって、空気ポンプ3は
停止される。
When the inside of the sealed tank 1 reaches the eye level, this is detected by the shortest l/-1 electrode rod 13cIS, and the air pump 3 is stopped by the signal output from the level sensor 9.

ところで、魚槽30中の角氷の混合比率よりも、サクシ
ョンポース12に吸揚げられる角氷の混今比串/I′i
通常濃度が薄くなる傾向となる。それは、魚体の長さが
サクションホース12の[1径よす大となる場合は、特
にサクションホース先端の吸込11部分で水よゆも魚体
に抵抗かかかり、水の通過よりも魚体の通過に時間を要
する為であり、魚槽30内へ若12の補給水を加えなけ
れば、魚槽の角氷濃度が彌〈なり週ぎて最後には空気を
吸わせるようになる。この欠点は、移送管25の端部に
設けられた水切セパレータ24で水切りされた水の一部
を還水ホ ス29によって元の魚槽30へ還水するよう
に構成することによって除去される。
By the way, the mixing ratio of ice cubes sucked into the suction port 12 is higher than the mixing ratio of ice cubes in the fish tank 30.
Normally, the concentration tends to become thinner. If the length of the fish body is one diameter larger than the suction hose 12, the water will resist the fish body, especially at the suction 11 part at the tip of the suction hose, and the passage of the fish body will be more difficult than the passage of water. This is because it takes time, and unless supplementary water is added to the fish tank 30, the concentration of ice cubes in the fish tank will drop and eventually the ice cubes will start to suck air. This drawback can be eliminated by configuring a structure in which a part of the water drained by the drain separator 24 provided at the end of the transfer pipe 25 is returned to the original fish tank 30 by the return water hose 29. .

ただ常に水切りされた液体の全量を魚槽30へ還せば次
第に魚槽30内の角氷濃度が下り最後には水ばかりとな
り、サクションホース12によって吸込ませるのに化種
(が悪くなるので還水ホースに連結された流液調整弁3
1の開明を調整し、あるいは溜槽28の液面レベルを調
整することによって、揚魚mに応じて、−一部の水を還
水するのがよい。
However, if you always return the entire amount of the drained liquid to the fish tank 30, the concentration of ice cubes in the fish tank 30 will gradually decrease and eventually there will be only water. Flow control valve 3 connected to water hose
It is preferable to return some of the water depending on the number of fish m to be lifted by adjusting the opening of 1 or the liquid level of the reservoir tank 28.

魚槽30中の魚最の約80〜90%位は、上記の運転方
法で揚魚できるが、魚槽内の角氷量が更に減少すれば、
サクションホース12のI)k 込[’j ヲ魚の密集
部に移動しなければならないが、この作業中に若モの空
気を吸込ませたり、又還水を魚槽中へ返戻する場合にそ
の還水と共に気泡状の空気が角氷の中に混入する。よっ
てその気?f!l空気もサクションホース12によって
1吸揚げられた密閉タンク1の角氷レベルは次第に低下
する。
Approximately 80 to 90% of the fish in the fish tank 30 can be raised using the above operating method, but if the amount of ice cubes in the fish tank decreases further,
The suction hose 12 must be moved to an area where the fish are densely populated, but during this process, the air from the young fish must be sucked in, and when return water is returned to the fish tank, the return water must be removed. Bubbles of air get mixed into the ice cubes along with the water. So do you want to do that? f! The level of ice cubes in the closed tank 1, in which air is also sucked up by the suction hose 12, gradually decreases.

121  密閉タンク1内の角氷レベルが中間水飴検出
まで低下すると、このことがレベルセン+/′9で検出
すれ、レベルセンサ9の信号によって空気ポンプ3が再
起動される。空気ポンプ3は前回と同様上限水位検出で
停止する。この状態にあってもロータリ一式ポンプ20
は連続的に運転され、空気ポンプ3が!fiJ欠的に排
列運転される状態で、約80〜90%位度の揚魚まで可
能である。史に角氷電が少なくなれば、サクションホー
ス12に吸人いれる空気量が増加する。この状態となる
と、空気ポンプ3を併動運転しても吸込まれる空気量か
空気ポンプのり[ミ気量よりも犬となり、密閉タンク1
内の角氷にが中間水位検出位置よりも数丁する1、よっ
て、液面レベルがF限水位検出位置に至れば、このこと
が最も長い電極体13ぎに検出され、レヘルセンザ9の
出力信号によってロータリ一式固形物ポンプ20の運転
は停止され、空気ボ/ブ3のみの酢独運転となる。途中
密閉タンク1内が、中間水位検出位置まで1−昇すれば
、ロータリ一式固形物ポンプ20を再起動し、空気ポン
プ3とロータリ一式固形物ポンプ20とを併動運転し、
に限水位で空気ポンプ3を停十、し、ロータリ一式固形
物ポンプ20の屯独運転となることは前記と同様である
121 When the ice cube level in the closed tank 1 drops to the intermediate syrup detection level, this is detected by the level sensor +/'9, and the air pump 3 is restarted by the signal from the level sensor 9. The air pump 3 stops when the upper limit water level is detected, as in the previous case. Even in this state, the rotary complete pump 20
is operated continuously, and air pump 3! When the fiJ is operated intermittently, it is possible to catch about 80 to 90% of the fish. As the number of ice cubes decreases, the amount of air sucked into the suction hose 12 increases. In this state, even if the air pump 3 is operated in parallel, the amount of air sucked in or the amount of air sucked will be greater than the amount of air in the sealed tank 1.
The ice cube inside is a few feet above the intermediate water level detection position. Therefore, when the liquid level reaches the F limit water level detection position, this is detected at the longest electrode body 13, and the output signal of the level sensor 9 is As a result, the operation of the rotary solids pump 20 is stopped, and only the air tube 3 is operated in a vacuum. When the inside of the sealed tank 1 rises to the intermediate water level detection position, the rotary solids pump 20 is restarted, and the air pump 3 and the rotary solids pump 20 are operated in parallel.
As described above, the air pump 3 is stopped at the water limit level and the rotary solids pump 20 is operated independently.

この場合ソ1り気の吸込量が非常に多くて、ロータリ一
式固形物ポンプ20の運転時間が短かくなれば、ロータ
リ一式固形物ポンプの運転を完全に停止し、密閉タンク
式固形物ポンプの運転に切換える。
In this case, if the intake amount of air is very large and the operation time of the rotary solids pump 20 is shortened, the operation of the rotary solids pump 20 is completely stopped and the closed tank solids pump is turned off. Switch to driving.

[81密閉タンク式固形物ポンプの運転は、ロータリ一
式固形物ポンプ20を停止して空気ポンプ3のみを運転
し、密閉タンク1内の角氷しヘルの1−限で四方切換弁
2を第1図の点線位置に切換えることにより、空気ポン
プは大気を吸入して密閉タンク1内へ圧縮寮気を圧入す
る。その空気の圧力によって角氷が加圧され、吸入側の
llf+l・弁5は閉止され、角氷はロータリ一式固形
物ポンプ201+IK ’tlf、 人し、ロータリ一
式固形物ポンプ20のロータ18及びケーシング17内
を通過し、吐出側逆上弁6及び移送@−25を通って水
切セパレータ24に搬送される。
[81 To operate the closed tank type solids pump, the rotary solids pump 20 is stopped, only the air pump 3 is operated, and the four-way switching valve 2 is turned on at the 1st limit of ice cube heating in the closed tank 1. By switching to the dotted line position in FIG. 1, the air pump sucks in atmospheric air and pressurizes compressed dormitory air into the sealed tank 1. The ice cubes are pressurized by the pressure of the air, the llf+l valve 5 on the suction side is closed, and the ice cubes are transferred to the rotary solids pump 201 + IK'tlf, the rotor 18 of the rotary solids pump 20, and the casing 17. The water passes through the inside, and is conveyed to the drain separator 24 through the discharge side reversal valve 6 and the transfer@-25.

この場合ロータリ一式固形物ポンプ20は回転していな
いが、都合の良いことには固形物が水と共にai+Jし
てもその通過方向に対して円滑に方向が転換さねるよう
にロータやケーシングが形成されるので魚体を傷めるこ
とがない。更に又、サタンヨンホース12から角氷と共
に大量の空気が吸入されるが、その空気の混入によって
も、この密閉タンク式固形物ポンプでは魚体が傷められ
ることもない。
In this case, the rotary solids pump 20 is not rotating, but the rotor and casing are conveniently formed so that even if the solids and water ai+J, the direction of the solids does not change smoothly with respect to the direction of passage. , so there is no damage to the fish body. Furthermore, although a large amount of air is sucked in from the satanyong hose 12 together with the ice cubes, this closed tank type solids pump does not cause any damage to the fish body even if the air is mixed in with the ice cubes.

141  吐出行櫟は密閉タンク1内の下限レベル検出
まで続けられ、下限レベル検出によって四方切換弁2は
元の第1図の実線位置に切換えられ、吐出側逆上弁6は
閉止、吸入側逆上弁5が開に1シ、再び吸入行程に移行
する。以下これを繰り返し、魚槽30が完全に空になる
捷で運転される。
141 The discharge flow continues until the lower limit level is detected in the sealed tank 1, and upon detection of the lower limit level, the four-way switching valve 2 is switched to the original position shown in the solid line in FIG. 1, the discharge side reversing valve 6 is closed, and the suction side is reverse When the upper valve 5 is opened, the suction stroke begins again. Thereafter, this process is repeated until the fish tank 30 is completely emptied.

1−紀の運転方法の能、魚体が片口いわし等で非常に小
さい場合は、次の方法による運転が好ましい0 サクションホース12の口径より魚体の長さが小さい場
合は、吸込口部分で魚体かほとんと抵抗を受けないので
、非常に濃度が高く吸入され、σ]槽中の角氷比率と変
らない状態で1汲人された柔かい魚体は高速で回転する
ロータリ一式固形物ポンプ20の運転によって揚魚され
て魚体が傷められる恐れがある。よって、最初は密閉タ
ンク式固形物ポンプを運転して、水切セパレータ24の
還水を全量魚槽30に返戻し、魚槽30の色水濃度か、
ある低度数丁して希薄になってからロータリ一式固形物
ポンプを運転するようにすればよい。それは色水濃度が
イ迩端に濃い状態では魚体との間のクッションになる水
が少なく直接魚体同士かすれ合うことによって生ずる魚
体の損傷か発生ずるからである。
If the fish is very small, such as a single-mouthed sardine, it is preferable to operate using the following method.0 If the length of the fish is smaller than the diameter of the suction hose 12, the suction port will cut the fish. Since it encounters almost no resistance, it is inhaled at a very high concentration, and the soft fish body, which has been pumped up in a state that does not differ from the ice cube ratio in the tank, is pumped by the operation of the rotary solids pump 20 that rotates at high speed. There is a risk that the fish body may be damaged by being fried. Therefore, at first, the closed tank type solids pump is operated to return all of the water from the drain separator 24 to the fish tank 30, and the concentration of colored water in the fish tank 30 is determined.
The rotary solids pump can be operated only after the liquid is diluted to a certain degree. This is because when the colored water is extremely concentrated, there is less water to act as a cushion between the fish and the fish, causing damage to the fish as a result of the fish directly brushing against each other.

I−記のように、先に密閉タンク式固形物ポンプを運転
することによ・リロータリ一式固形物ポンプ20の中の
空気が完全に排出されてからロータリ一式固形物ポンプ
20の運転が出来るので、単一、’iTi路のロータを
有するロータリ一式固形物ポンプを使用するのに好適で
ある。それはロータリ一式固形物ポンプ20を運転する
場合、例え少しの空気でイ、ロータ内に残ったまま運転
すると、ポンプ作用かなされないので、魚体が空回りし
て傷付きか発生ずるのみならず、ロータが動的アンバラ
ンスとなり激しい振動を生ずる為、軸受部、グランドシ
ール部を傷め易くその振動に耐える大径のシャフトや軸
受けを使用すれば、ある程度の防11・、はできるが、
不経済である。ブレードレスロータの?11J−−−−
曲路の一枚羽根のものを使用するとその傾向か構造的に
も特に顕著で著しくその寿命を短縮するものである。と
ころか密閉タンク式固形物ポンプを運転することにより
ロータ内へ角氷が圧入されるので完全に空気か排出され
るからである。
As shown in I-, by first operating the closed tank solids pump, the rotary solids pump 20 can be operated after the air inside the rerotary solids pump 20 is completely exhausted. , is suitable for use with a rotary complete solids pump having a single, 'iTi-way rotor. When operating the rotary solids pump 20, even if a small amount of air is left in the rotor, the pump will not work, which will not only cause the fish body to spin idly and cause damage, but also cause the rotor to become damaged. This can be prevented to some extent by using a large-diameter shaft or bearing that can withstand the vibrations, which can easily damage the bearings and gland seals as it causes dynamic imbalance and generates severe vibrations.
It is uneconomical. Bladeless rotor? 11J---
If a single-bladed blade with a curved path is used, this tendency is particularly noticeable from a structural standpoint, and its life will be significantly shortened. On the other hand, since the ice cubes are forced into the rotor by operating the closed tank type solids pump, the air is completely exhausted.

0゛)効果 本発明の固形物移送装置は、前記の構成によって従来の
いかなる固形物移送装置も実現し得なかった低損傷高移
送能力という極めて困難とされた難問を解消した。この
特性によって、永年の間強く要求されてきた多種多様の
用途に於る種々雑多な悪条件−ドでのノ#(想的な移送
特性を実現し、固形物移送を省力化、高能串化、安全化
、高速化するという数々のり効を奏するのである。
0゛) Effect The solid material transfer device of the present invention solves the extremely difficult problem of low damage and high transfer capability, which has not been possible with any conventional solid material transfer device, due to the above-described structure. This characteristic enables the realization of ideal transfer characteristics under various adverse conditions in a wide variety of applications, which have been strongly demanded for many years, and enables labor-saving and high-performance skewers for solid material transfer. It has a number of benefits, including increased safety and speed.

この優れた特性は、ロータリ一式固形物ポンプと密閉タ
ンク式固形物ポンプとを直列に連結し、しかも密閉タン
ク式固形物ポンプをロータリ一式固形物ポンプの吸入側
に連結する構成によって実現される。即ちこの構成によ
ると、ロータリ一式固形物ポンプでもって固形物を11
旨中よく単位時間に多量に移送でき、しかも万一空気を
吸入したとしても、この空気は密閉タンク式固形物ポン
プの密閉タンクで除去され、これによってロ−タリ一式
固形物ポンプの空気による空転を極減でき、更に、この
密閉タンクは、ロータリー・式固形物ポンプを停止1−
シて液体を吸入、排出することによっても固形物の移送
ができる為に外ならない。
This excellent characteristic is achieved by a configuration in which a rotary solids pump and a closed tank solids pump are connected in series, and the closed tank solids pump is connected to the suction side of the rotary solids pump. That is, according to this configuration, solids are pumped 11 times using a rotary solids pump.
In fact, it is possible to transfer a large amount per unit time, and even if air is inhaled, this air is removed in the closed tank of the closed tank type solids pump, which prevents the rotary solids pump from idling due to air. Furthermore, this sealed tank allows you to stop the rotary solids pump.
Solid matter can also be transferred by sucking in and discharging liquid.

史に、従来のロータリ一式固形物ポンプは、使用時に空
気を吸入しないように、水中ポンプとして使方Jされる
ことか多く、大きくて重いポンプ全体を水中に吊り込む
必要があったか、本発明の固形物移送装置は、ロータリ
一式固形物ポンプが空気を1吸入することか構造1−極
減される為、ポンプ本体を水中に吊り込む必要がなく、
単にサクションボースを水中に挿入するたけで取り扱い
易くして便利にしかも安全に使用できる等の効果もある
Historically, conventional rotary solids pumps were often used as submersible pumps to avoid inhaling air during use. The solids transfer device has a structure in which the rotary solids pump only takes in air once, so there is no need to suspend the pump body into the water.
It has the advantage of being easy to handle, convenient and safe to use simply by inserting the suction bow into the water.

又、本発明の固形′物の移送装置は、多桁の空気を吸入
し易い状態で使用されるとき、あるいは固形物濃度か高
くロータリ一式固形物ポンプでは移送時の損傷が多い場
合、ロータリ一式固形物ポンプの運転を停止して密閉タ
ンク式固形物ポンプでもって固形物を傷イ」き少なく移
送できる。このとき、1n形物はロータリ一式固形物ポ
ンプのロータ内を通過するが、ロータリ一式固形物ポン
プはロータに固形物の移送通路が形成される為、ロータ
リ一式固形物ポンプを通過するときに固形物か損傷され
ることはなく、固形物は最も傷付き少なく移送できる。
Furthermore, when the solid material transfer device of the present invention is used in a state where multiple digits of air are easily inhaled, or when the solids concentration is high and a rotary set solid pump is often damaged during transfer, The operation of the solids pump is stopped and the solids can be transferred with a closed tank type solids pump with less damage. At this time, the 1N-type object passes through the rotor of the rotary one-piece solids pump, but since the rotary one-piece solids pump has a solids transfer passage formed in the rotor, the solids pass through the rotary one-piece solids pump. No objects are damaged, and solid objects can be transported with the least damage.

更に、本発明の固形物移送装置は、運転を停止した状態
で固形物がスムーズに通過できる密閉タンク代置形物ポ
ンプ七ロータリ一式固形物ポンプとを直列に連結する。
Further, the solids transfer device of the present invention connects in series a sealed tank replacement type pump and seven rotary solids pumps through which solids can pass smoothly even when the operation is stopped.

この為、ポンプの運転状態の切換か自由で、−万のポン
プをj重転しながら1mのポンプを起動し、あるいはσ
1ηポンプを同時に運転することゼ)可能である。更に
、両ポンプを切り換えるときに配管の変更等は全く必要
なく、モータ等の運転を制御するたけで運転状態を簡単
かつ容易に、しかも迅速に切り換えられる等数々の卓効
を実現する。
For this reason, you can freely switch the operating state of the pump, starting up the 1m pump while rotating the -10,000 pumps, or starting the 1m pump while σ
It is possible to run 1η pumps at the same time. Furthermore, when switching between the two pumps, there is no need to change the piping at all, and by simply controlling the operation of the motor, etc., the operating state can be easily and quickly switched, and many other advantages are realized.

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

第1図は本発明の一実施例を示す固形物の移送装置の概
略断面図、第2図は密閉タンク底部の水平断面図、第3
図ないし第5図は密閉タンクの垂直断面図、第6図は也
の実施例を示す固形物の移送装置の概略断面図、第7図
および第8図はロータリ一式固形物ポンプの断面図、第
9図および)第10図はロータの断面図である。 1・・密閉タンク、2・・四方切換弁、3・・空気ポン
プ、4・・吸入口、5・・逆止弁、6・・逆11−弁、
7・・排出[1,8・・空気口、9・・レベルセンセ、
10・・排出管、11・・吸入ダクト、12・・→かク
ションホース、13・・電極棒、14・・吸入管、15
・・吸気口、16・・多孔&、17・・ケーシング、1
8・・ロータ、19・・吸入口、20・・ロータリ一式
固形物ポンプ、21・・送出口、22・・回転軸、23
・・通過路、24・・水切セパレータ、25・・移送管
、26・・受箱、27・・選別価、28・・溜槽、29
・・還水ホース、30・・魚槽、31・・流量調整弁、
32・・通路、33・・分岐管、34・・排気管、 出願人  林   武 第  2  図 第  4  図 第  6  図 第、7図 1
FIG. 1 is a schematic cross-sectional view of a solid material transfer device showing an embodiment of the present invention, FIG. 2 is a horizontal cross-sectional view of the bottom of a closed tank, and FIG.
5 to 5 are vertical sectional views of a closed tank, FIG. 6 is a schematic sectional view of a solids transfer device showing another embodiment, FIGS. 7 and 8 are sectional views of a rotary solids pump, 9 and 10 are cross-sectional views of the rotor. 1. Sealed tank, 2. Four-way switching valve, 3. Air pump, 4. Inlet, 5. Check valve, 6. Reverse 11-valve.
7. Exhaust [1, 8. Air vent, 9. Level sense,
10...Discharge pipe, 11...Suction duct, 12...→action hose, 13...Electrode rod, 14...Suction pipe, 15
・・Intake port, 16・・Porous &, 17・・Casing, 1
8... Rotor, 19... Suction port, 20... Rotary complete solids pump, 21... Outlet port, 22... Rotating shaft, 23
...Passing path, 24.. Drain separator, 25.. Transfer pipe, 26.. Receiving box, 27.. Sorting price, 28.. Reservoir, 29.
・・Return water hose, 30・・Fish tank, 31・・Flow rate adjustment valve,
32...Passway, 33...Branch pipe, 34...Exhaust pipe, Applicant Takeshi Hayashi Figure 2 Figure 4 Figure 6 Figure 7 Figure 1

Claims (1)

【特許請求の範囲】 (+)  固形物移送装置は密閉タンク式固形物ポンプ
と、ロータリ一式固形物ポンプとを備えており、密閉夕
/り式固形物ポンプは密閉タンクと、減圧手段と、1及
人弁と、排出弁とを備え、密閉タンクは、固1し物の通
路と空気t−1とが開[Iされており、減圧毛段は密閉
タンク内の空気を排気するように、吸入側か密閉タンク
の空気[]に連通されており、吸入弁は固形物混合の液
体が密閉タンク内に吸入される工程においてのみ開弁す
る弁で、この吸入弁は密閉タンクの通路に連通ずる吸入
fl管路に連結されており、排出′frは、12i1形
物混合の液体が密閉タンク力・らすU出される工程に於
てのみ開弁する弁て、密閉タンクの通路に連通する吐出
(lll!管路に連結されており、前記密閉タンク式固
形物ポンプとロータリー゛式固形物ポンプとはrH,い
に直列に連結されており、かつ、ロータリ一式固形物ポ
ンプの吸入(1[1か密閉タンクの吐1.(l (Ii
t1通路に連通されており、固形物が、密閉タンクをj
m過した凌jJ−クリ一式固形物ポンプのインペラ内を
通過して移送されるように構成されている固形物の移送
装置Ft 。 (2)密閉タンクに2個の通路が開[lされ、−力の通
路は吸入IT、lで、池の−Hの通路がu1出11て、
1.lIり人[−1は吸入弁に連通され、排出[1には
ロータリ一式固形物ポンプの吸入側が連結されている特
許請求の範囲第(1)項記載の固形物の移送装置i″t
。 (3)密閉タンクの通路がひとつで、この通路が吸入[
−1とtJ++ trl rlとに2分岐され、吸入口
は1汲人弁に、排出[1はロータリ一式1〜形物ポンプ
に連aされている特許請求の範囲第(1)項記載の固形
物の移送装置。 (4)排出弁がロータリ一式固形物ポンプの吐出011
1に連結されている特許請求の範囲第(1)項記載の固
形物の移送装置。 (5)吸入弁と排出弁とが逆止弁である特許請求の範囲
第(1)項記載の固形物の移送装置。 (6)密閉タンクがレベルセンサを備え、このレベルセ
ンサが減圧手段とロータリ一式固彫物ポンプの運転を制
御し、密閉タンクの液体レベルが一定量1−のときにロ
ータリ一式固形物ポンプが運転される特許請求の範囲第
(1)項記載の固形′物の移送装置。 (7)  ロータリ一式固形物ポンプと密閉タンクとの
間に減圧手段の吸入側が連通され、減圧手段でもってロ
ータリ一式固形物ポンプと密閉タンクとの間に流入する
空気が排出されるように構成されている特許請求の範囲
第(1)項記載の固形物の移送装置。 (8)  ロータリ一式固形物ポンプがブレードレスロ
ータラ備えるブレードレスローターポンプで、このロー
タは、分岐されない単一通路を備える特許請求の範囲第
(1)項記載の固形物の移送装置。 (9)  ロータリ一式固形物ポンプが密閉夕゛・りよ
り下に配設されている特許請求の範囲第(1)項記載の
固形物の移送装置。
[Claims] (+) The solids transfer device includes a closed tank type solids pump and a rotary combined solids pump, and the closed and double type solids pump includes a closed tank, a pressure reducing means, The airtight tank is equipped with an airtight valve and a discharge valve, and the airtight tank is opened so that the solid matter passage and the air t-1 are opened, and the decompression stage is configured to exhaust the air in the airtight tank. , the suction side is connected to the air in the sealed tank, and the suction valve is a valve that opens only during the process in which liquid mixed with solids is sucked into the sealed tank, and this suction valve is connected to the passage of the sealed tank. It is connected to the suction fl pipe which communicates with the tank, and the discharge 'fr is connected to the passage of the closed tank through a valve that opens only during the process in which the liquid mixed with 12I1 is discharged from the closed tank. The closed tank type solids pump and the rotary type solids pump are connected in series, and the rotary type solids pump's suction ( 1 [1 or the discharge of a closed tank 1.(l (Ii
It is connected to the t1 passage, and the solids are passing through the closed tank.
A solids transfer device Ft configured to be transferred through an impeller of a solids pump. (2) Two passages are opened in the closed tank, the -force passage is inlet IT, l, and the pond -H passage is u1 exit 11,
1. The solid material transfer device i''t according to claim (1), wherein the solid material transfer device i''t is connected to the suction valve, and the discharge port [1 is connected to the suction side of a rotary solid material pump.
. (3) There is one passage in the sealed tank, and this passage is used for the intake [
-1 and tJ++ trl rl, the suction port is connected to the pump valve 1, and the discharge port [1 is connected to the rotary set 1 to the solid pump a]. Equipment for transporting objects. (4) The discharge valve is the discharge 011 of the rotary solids pump.
1. A solid material transfer device according to claim 1, which is connected to a solid material transfer device. (5) The solid material transfer device according to claim (1), wherein the suction valve and the discharge valve are check valves. (6) The sealed tank is equipped with a level sensor, and this level sensor controls the operation of the pressure reducing means and the rotary solid material pump, and when the liquid level in the sealed tank is a certain amount 1-, the rotary solid material pump is operated. A solid material transfer device according to claim (1). (7) The suction side of the pressure reducing means is communicated between the rotary solids pump and the sealed tank, and the air flowing between the rotary solids pump and the sealed tank is discharged by the pressure reducing means. A solid material transfer device according to claim (1). (8) The solids transfer device according to claim 1, wherein the rotary solids pump is a bladeless rotor pump having a bladeless rotor, and the rotor has a single unbranched passage. (9) The solid material transfer device according to claim (1), wherein the rotary solid material pump is disposed below the closed door.
JP57110243A 1982-06-25 1982-06-25 Solid material transfer device Granted JPS594524A (en)

Priority Applications (5)

Application Number Priority Date Filing Date Title
JP57110243A JPS594524A (en) 1982-06-25 1982-06-25 Solid material transfer device
IS2806A IS1413B6 (en) 1982-06-25 1983-05-17 Equipment and method of transporting goods, e.g. fish, in liquid
DK220783A DK220783A (en) 1982-06-25 1983-05-18 A DEVICE FOR SHIPPING OF SOLID OBJECTS
ES523568A ES8404944A1 (en) 1982-06-25 1983-06-23 Solid material transfer device
NO832324A NO157777C (en) 1982-06-25 1983-06-24 SOLID TRANSPORT DEVICE.

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP57110243A JPS594524A (en) 1982-06-25 1982-06-25 Solid material transfer device

Publications (2)

Publication Number Publication Date
JPS594524A true JPS594524A (en) 1984-01-11
JPH0362610B2 JPH0362610B2 (en) 1991-09-26

Family

ID=14530730

Family Applications (1)

Application Number Title Priority Date Filing Date
JP57110243A Granted JPS594524A (en) 1982-06-25 1982-06-25 Solid material transfer device

Country Status (5)

Country Link
JP (1) JPS594524A (en)
DK (1) DK220783A (en)
ES (1) ES8404944A1 (en)
IS (1) IS1413B6 (en)
NO (1) NO157777C (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4884091A (en) * 1987-10-08 1989-11-28 Nippon Seimitsu Kogyo Kabushiki Kaisha Exposure control device in a camera
NO20181478A1 (en) * 2018-11-19 2020-05-20 Mjoes Metallvarefabrikk As Piping fish pump

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109573486B (en) * 2018-11-15 2021-09-24 山东理工大学 Harmless conveyor of fish and shrimp

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4916954U (en) * 1972-05-18 1974-02-13
JPS56108622A (en) * 1980-02-01 1981-08-28 Kyoei Zoki Kk Transfer device for solid material
JPS5757123A (en) * 1980-09-16 1982-04-06 Kyoei Zoki Kk Solid matter transfer apparatus

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4916954U (en) * 1972-05-18 1974-02-13
JPS56108622A (en) * 1980-02-01 1981-08-28 Kyoei Zoki Kk Transfer device for solid material
JPS5757123A (en) * 1980-09-16 1982-04-06 Kyoei Zoki Kk Solid matter transfer apparatus

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4884091A (en) * 1987-10-08 1989-11-28 Nippon Seimitsu Kogyo Kabushiki Kaisha Exposure control device in a camera
NO20181478A1 (en) * 2018-11-19 2020-05-20 Mjoes Metallvarefabrikk As Piping fish pump
NO344928B1 (en) * 2018-11-19 2020-07-06 Mjoes Metallvarefabrikk As Piping fish pump

Also Published As

Publication number Publication date
DK220783A (en) 1983-12-26
NO832324L (en) 1983-12-27
IS1413B6 (en) 1990-01-29
ES523568A0 (en) 1984-05-16
JPH0362610B2 (en) 1991-09-26
DK220783D0 (en) 1983-05-18
IS2806A7 (en) 1983-12-26
NO157777C (en) 1988-05-25
NO157777B (en) 1988-02-08
ES8404944A1 (en) 1984-05-16

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