JPH0786360B2 - Liquid pumping equipment - Google Patents
Liquid pumping equipmentInfo
- Publication number
- JPH0786360B2 JPH0786360B2 JP63029921A JP2992188A JPH0786360B2 JP H0786360 B2 JPH0786360 B2 JP H0786360B2 JP 63029921 A JP63029921 A JP 63029921A JP 2992188 A JP2992188 A JP 2992188A JP H0786360 B2 JPH0786360 B2 JP H0786360B2
- Authority
- JP
- Japan
- Prior art keywords
- liquid
- vacuum chamber
- pipe
- pumping
- 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.)
- Expired - Fee Related
Links
- 239000007788 liquid Substances 0.000 title claims description 112
- 238000005086 pumping Methods 0.000 title claims description 64
- 238000007599 discharging Methods 0.000 claims description 6
- 230000006837 decompression Effects 0.000 claims description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 56
- 238000011084 recovery Methods 0.000 description 14
- 238000007667 floating Methods 0.000 description 11
- 239000007789 gas Substances 0.000 description 6
- 238000000034 method Methods 0.000 description 5
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 4
- 238000007726 management method Methods 0.000 description 4
- 239000003595 mist Substances 0.000 description 4
- 239000001301 oxygen Substances 0.000 description 4
- 229910052760 oxygen Inorganic materials 0.000 description 4
- 238000005273 aeration Methods 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 230000005484 gravity Effects 0.000 description 3
- 239000012535 impurity Substances 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 239000004576 sand Substances 0.000 description 3
- 239000007787 solid Substances 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 230000002950 deficient Effects 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 230000002093 peripheral effect Effects 0.000 description 2
- 239000003245 coal Substances 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 239000013049 sediment Substances 0.000 description 1
- 239000002689 soil Substances 0.000 description 1
- 239000011343 solid material Substances 0.000 description 1
Landscapes
- Jet Pumps And Other Pumps (AREA)
Description
【発明の詳細な説明】 〔産業上の利用分野〕 この発明は、土砂等の固形物が混在している液体を、こ
の液体の液面に浮かぶ浮遊物とともに高所に汲み揚げる
ことのできる液体の汲み揚げ装置に関するものである。The present invention relates to a liquid capable of pumping a liquid containing a solid substance such as earth and sand to a high place together with a floating substance floating on the liquid surface of the liquid. The present invention relates to a pumping device.
土砂等を含む水の汲み揚げを行うための汲み揚げ方法と
して、気泡ポンプを用いた方法がある。この気泡ポンプ
は炭鉱の坑道等の排水の目的で開発されたものであり、
水中深く差し込まれた汲み揚げ管下端の吸入口付近から
汲み揚げ管内に空気を圧入することによつて、汲み揚げ
管内に水と空気の混合体の上昇流を生じさせ、汲み揚げ
管の上端側に水を汲み揚げるようになつている。このよ
うな気泡ポンプを用いた方法では、ポンプがポンピング
経路中に設けられていないため、ポンピング流が通る汲
み揚げ管内に障害となるものがなく、土砂等の固形物を
含む水でも汲み揚げることができるという利点を有して
いる。しかしながら、その原理は、汲み揚げ管の下端か
ら汲み揚げ管内に空気を圧入することによつて、汲み揚
げ管内の水を、水と空気の混合状態にし、その混合体の
平均比重を水だけの比重よりも小さくすることにより、
水面よりも高い水柱を汲み揚げ管内に生じさせるという
ものである。そのため、上記のような気泡ポンプを用い
た方法では、揚水能力が汲み揚げ管の下端の液面下の深
さに制約され、充分な深さが確保できない場合には、そ
の使用が困難となる。したがつて、その用途は深井戸や
深い海底,湖底等に限定されるという問題がある。ま
た、汲み揚げ管内に生じる上昇流の速度が小さいため、
水とともに汲み揚げることのできる固形物はバラスト
(砂利)程度のものが限度であるという問題や、液面に
浮かぶ浮遊物を汲み揚げることができないという問題を
有している。As a pumping method for pumping water containing soil and the like, there is a method using a bubble pump. This bubble pump was developed for the purpose of draining the mines of coal mines,
By injecting air into the pumping pipe from near the suction port at the lower end of the pumping pipe deeply inserted in water, an upward flow of a mixture of water and air is generated in the pumping pipe, and the upper end side of the pumping pipe is It is designed to pump water. In such a method using a bubble pump, since the pump is not provided in the pumping path, there is no obstacle in the pumping pipe through which the pumping flow passes, and it is possible to pump up water containing solid matter such as earth and sand. It has the advantage that However, the principle is that the water in the pumping pipe is made into a mixed state of water and air by injecting air into the pumping pipe from the lower end of the pumping pipe, and the average specific gravity of the mixture is only water. By making it smaller than the specific gravity,
It is to draw a water column higher than the surface of the water and generate it in the lifting pipe. Therefore, in the method using the bubble pump as described above, the pumping capacity is restricted by the depth below the liquid surface at the lower end of the pumping pipe, and if the sufficient depth cannot be secured, its use becomes difficult. . Therefore, its use is limited to deep wells, deep seabeds, lake bottoms, etc. Also, since the speed of the upward flow generated in the pumping pipe is small,
There is a problem that the amount of solids that can be pumped up with water is about ballast (gravel), and that floating substances floating on the liquid surface cannot be pumped up.
このため、特開昭62−195498号公報に示す装置が提案さ
れている。すなわち、この装置は、下端開口が第1の液
体内に浸漬している入口部分と、フラツプ弁付き下端開
口が第2の液体内に浸漬している出口部分と、これら両
部分の上端開口同士を連結する頂点装置とからなる導管
を備えており、上記入口部分の下端開口内に空気を圧入
するため空気圧縮機および送出ラインを設けている。ま
た、上記頂点装置にガス受け室を設け、このガス受け室
にあけた吸込口を吸込ポンプに連通するとともに上記吸
込口を開閉する弁部材を上記頂点装置内に配設するよう
にしている。For this reason, the device disclosed in Japanese Patent Laid-Open No. 62-195498 has been proposed. That is, this device has an inlet portion whose lower end opening is immersed in the first liquid, an outlet portion whose lower end opening with a flap valve is immersed in the second liquid, and upper end openings of these two parts. And an air compressor and a delivery line for injecting air into the lower end opening of the inlet portion. Further, a gas receiving chamber is provided in the apex device, and a valve member for communicating the suction port opened in the gas receiving chamber with a suction pump and opening / closing the suction port is arranged in the apex device.
この装置を用い、つぎのようにして液体の汲み揚げが行
なわれる。すなわち、最初の状態では、導管内は大気圧
であるため入口部分内の液面および出口部分内の液面は
その外側の液面と同じ高さになつている。ついで、吸込
ポンプを始動させると、導管内の圧力が減少し、上記入
口部分内の液面および出口部分内の液面は引き上げられ
る。そののち、または上記吸込ポンプの始動と同時に、
空気圧縮機を始動させ、この空気圧縮機から加圧空気を
送出ラインを通して上記入口部分の下端開口内に圧入す
る。これにより、上記入口部分内の液体の有効密度が減
少し、入口部分内の液面はさらに引き上げられる。この
とき、上記入口部分の下端開口内に圧入された空気は泡
となつて上記入口部分内の第1の液体中を上昇したのち
上記頂点装置内に入りガス受け室から吸込ポンプに吸い
込まれる。やがて、上記入口部分内の液面は頂点装置に
達し、そののち、頂点装置を通つて出口部分に流れ込
み、出口部分内の液面とつながり、これにより上記入口
部分,頂点装置および出口部分に連続した液体の通路が
確立されるようになる。このようにして液体の通路が確
立された後は、上記頂点装置内で液面の平衡液面が維持
されるように弁部材が上記ガス受け室にあけた吸込口を
開閉して適正なガス抜きを行う。この装置によれば、上
記気泡ポンプを用いる方法よりも、揚水能力を大幅に向
上させることができるようになる。Using this device, the liquid is pumped up as follows. That is, in the initial state, since the inside of the conduit is at atmospheric pressure, the liquid surface in the inlet portion and the liquid surface in the outlet portion are at the same height as the outer liquid surface. Then, when the suction pump is started, the pressure in the conduit is reduced, and the liquid level in the inlet part and the liquid level in the outlet part are raised. After that, or at the same time when the suction pump is started,
The air compressor is started and pressurized air is forced from the air compressor through the delivery line into the lower opening of the inlet section. As a result, the effective density of the liquid in the inlet portion is reduced, and the liquid level in the inlet portion is further raised. At this time, the air press-fitted into the lower end opening of the inlet portion becomes bubbles and rises in the first liquid in the inlet portion, then enters the apex device and is sucked into the suction pump from the gas receiving chamber. Eventually, the liquid surface in the inlet portion reaches the apex device, and then flows through the apex device to the outlet portion and is connected to the liquid surface in the outlet portion, thereby continuing the inlet portion, the apex device and the outlet portion. The liquid passage will be established. After the passage of the liquid is established in this way, the valve member opens and closes the suction port opened in the gas receiving chamber so that the equilibrium liquid level in the apex device is maintained. Pull out. According to this device, the pumping capacity can be significantly improved as compared with the method using the bubble pump.
ところが、上記装置では、導管の入口部分の下端開口内
に加圧空気を圧入するために、上記加圧空気を発生させ
る空気圧縮機、および、この加圧空気を上記入口部分の
下端開口内にまで送出する送出ラインを設けることが必
要となり、装置が高価になり、その構造が複雑噛するう
え、装置全体が大形化する。しかも、管状に形成された
入口部分の下端部を真下に向けて第1の液体内に突入さ
せているため、下端開口から液体を汲み揚げるときに、
この液体とともに液面に浮かぶ浮遊物をも一緒に汲み揚
げることが殆どできない。さらに、管状に形成された出
口部分を下向きに延ばし、その下端開口にフラツプ弁を
取付けているため、出口部分の下端部が第2の液体内に
浸漬していない場合には、フラツプ弁が開いたときに上
記下端開口から出口部分内に気泡が侵入し、気泡および
液体が出口部分を逆上昇して頂点装置のガス受け室に流
入すると、ガス受け室の真空度が低下し、汲み揚げ量が
低下する。したがつて、第2の液体を収容する収容槽の
設置位置や収容槽内の液面位置を管理しなければなら
ず、管理面が複雑化する。However, in the above device, in order to pressurize the compressed air into the lower end opening of the inlet portion of the conduit, the air compressor that generates the compressed air, and the compressed air into the lower end opening of the inlet portion. It is necessary to provide a delivery line for delivering up to, the apparatus becomes expensive, the structure is complicated, and the entire apparatus becomes large. Moreover, since the lower end of the inlet portion formed in a tubular shape is projected right below to the inside of the first liquid, when pumping the liquid from the lower end opening,
Floating matter floating on the liquid surface with this liquid can hardly be pumped up together. Further, since the tubular outlet portion is extended downward and the flap valve is attached to the lower end opening, the flap valve opens when the lower end portion of the outlet portion is not immersed in the second liquid. When air bubbles intrude into the outlet from the lower end opening and the bubbles and liquid rise upward in the outlet and flow into the gas receiving chamber of the apex device, the degree of vacuum in the gas receiving chamber decreases and the pumping amount is increased. Is reduced. Therefore, it is necessary to manage the installation position of the storage tank for storing the second liquid and the liquid level position in the storage tank, which complicates the management surface.
そこで、特開昭55−64200号公報に示す装置が提案され
ている。この装置は、水底(例えば、地下隧道の底部)
に沈澱した土砂や泥水を高所へ吸い上げるための装置で
あり、真空ポンプと、これに連通する回収用真空タンク
と、この真空タンクから下方に延びる吸い上げ管とを備
えており、この吸い上げ管の先端部に吸い込み金具を有
するフレキシブル管を取付け、上記吸い込み金具し絞り
弁付きの空気導入管を設けるようにしている。この装置
は、空気圧縮機や送出ライン等を設けていないため、安
価で、構造が簡単化するうえ、装置全体が小形化する。Therefore, an apparatus disclosed in Japanese Patent Laid-Open No. 55-64200 has been proposed. This device is located at the bottom of the water (eg the bottom of an underground tunnel).
It is a device for sucking up sediment and mud water that have settled to a high place, and is equipped with a vacuum pump, a recovery vacuum tank that communicates with this, and a suction pipe that extends downward from this vacuum tank. A flexible pipe having a suction fitting is attached to the tip portion, and the suction fitting is provided with an air introduction pipe with a throttle valve. Since this device does not have an air compressor, a delivery line, etc., it is inexpensive, the structure is simplified, and the entire device is downsized.
しかしながら、この装置は、水底に沈澱した土砂や泥水
を吸い上げる装置であり、そのため、吸い上げ管の先端
部に取付けたフレキシブル管の吸い込み金具を下方に向
けて泥水等内に突入させている。したがつて、吸い込み
金具の先端開口から泥水等を吸い込むときに、泥水等と
ともに水面に浮かぶ浮遊物を一緒に吸い上げることがで
きない。しかも、吸い上げ管で吸い上げた泥水等を真空
タンク内に溜めるため、真空タンク内の貯留量に限度が
ある。However, this device is a device for sucking up the earth and sand or muddy water that has settled on the bottom of the water, so that the suction fitting of the flexible pipe attached to the tip of the suction pipe is thrust downward into the muddy water or the like. Therefore, when sucking muddy water or the like through the tip opening of the suction metal fitting, it is not possible to suck up the suspended matter floating on the water surface together with the muddy water or the like. Moreover, since the muddy water sucked up by the suction pipe is stored in the vacuum tank, the storage amount in the vacuum tank is limited.
この発明は、このような事情に鑑みなされたもので、安
価で、しかも構造が簡単で、装置全体を小形化すること
ができ、さらに、液面に浮かぶ浮遊物を効率よく汲み揚
げることができ、そのうえ、管理面が簡素化された液体
の汲み揚げ装置の提供をその目的とする。The present invention has been made in view of the above circumstances, is inexpensive, has a simple structure, can be downsized the entire device, and can efficiently pump up suspended matter floating on the liquid surface. Moreover, it is an object of the present invention to provide a liquid pumping-up device whose management is simplified.
上記目的を達成するために、この発明の液体の汲み揚げ
装置は、液面上方に配設される密封状の真空室から液面
に向けて汲み揚げ管を配設し、上記真空室の天井部側
に、真空室内の空気を吸引することにより上記真空室内
を減圧する減圧手段を接続した液体の汲み揚げ装置であ
つて、上記汲み揚げ管の下端開口を液面近傍に開口する
とともに、この下端開口との間に所定間隔をあけた状態
で上記汲み揚げ管の下端部に皿状体を取付けてこの皿状
体を液面よりやや液中に入つた位置に配設し、上記真空
室内を減圧手段で減圧することにより、大気圧との差圧
による液柱を汲み揚げ管内に作るとともに、この液柱の
下端部に上記汲み揚げ管の下端部もしくは下端開口から
大気を自然流入させて上記真空室内に液体を汲み揚げ、
この真空室内に汲み揚げられた液体を外部に排出する排
出管を真空室の底部から下方に延ばし、上記排出管の下
端部をU字形に形成し、このU字形部分の端部に開口す
る排出口に、この排出口での圧力が大気圧以上になつた
状態で開いて排出管の液体を外部に排出しうる弁体を取
付けたという構成をとる。In order to achieve the above object, the liquid pumping apparatus of the present invention has a pumping pipe arranged from a sealed vacuum chamber arranged above the liquid surface toward the liquid surface, and a ceiling of the vacuum chamber. A pumping device for a liquid, which is connected to a pressure reducing means for depressurizing the inside of the vacuum chamber by sucking air in the vacuum chamber, wherein the lower end opening of the pumping pipe is opened near the liquid level, and A plate-like body is attached to the lower end of the pumping pipe with a predetermined distance from the lower end opening, and the plate-like body is arranged at a position slightly immersed in the liquid from the liquid surface, and the vacuum chamber By decompressing with a decompression means, a liquid column due to the pressure difference from the atmospheric pressure is created inside the pumping pipe, and the atmosphere is allowed to naturally flow into the lower end of the liquid column from the lower end or the lower end opening of the pumping pipe. Pumping liquid into the vacuum chamber,
A discharge pipe for discharging the liquid pumped up into the vacuum chamber to the outside is extended downward from the bottom of the vacuum chamber, the lower end portion of the discharge pipe is formed in a U shape, and the discharge pipe is opened at the end portion of the U shape portion. The outlet is provided with a valve element that is opened when the pressure at the outlet is equal to or higher than the atmospheric pressure and that is capable of discharging the liquid in the outlet pipe to the outside.
すなわち、この発明の液体の汲み揚げ装置は、液面上方
に排出される密封状の真空室から液面に向けて汲み揚げ
管を配設し、上記真空室の天井部側に、真空室内の空気
を吸引することにより上記真空室内を減圧する減圧手段
を接続するようにしている。そして、上記真空室内を減
圧手段を用いて減圧することにより、大気圧とその差圧
による液柱を上記汲み揚げ管内に作るとともに、この液
柱の下端部に大気を上記汲み揚げ管の下端部もしくは下
端開口から自然流入させて、真空室内に液体を汲み揚げ
るようにしている。このようにこの発明では、汲み揚げ
管の下端部もしくは下端開口から汲み揚げ管内の液柱に
大気を自然流入させるようにしているため、従来例(特
開昭62−195498号公報に示す装置)では必要であつた空
気圧縮機、および送出ラインが必要でなくなり、装置が
安価になり、その構造が簡単化するうえ、装置全体が小
形化する。しかも、汲み揚げ管の下端開口を液面近傍に
開口するとともに、この下端開口との間に所定間隔をあ
けた状態で上記汲み揚げ管の下端部に皿状体を取付けて
この皿状体を液面よりやや液中に入つた位置に配設して
いるため、上記皿状体の外周部から皿状体内に液体が勢
いよく流入し、この流入に伴い液面に浮かぶ浮遊物も皿
状体内に流入する。したがつて、上記皿状体内に流入し
た液体および浮遊物を、液面近傍に開口する汲み揚げ管
の下端開口から、効率よく汲み揚げることができるよう
になる。さらに、真空室内に汲み揚げられた液体を外部
に排出する排出管を真空室の底部から下方に延ばし、上
記排出管の下端部をU字形に形成し、このU字形部分の
端部に開口する排出口に、この排出口での圧力が大気圧
以上になつた状態で開いて排出管の液体を外部に排出し
うる弁体を取付けているため、真空室内を減圧すると弁
体が排出口を閉じて真空室内が密封状態になり、また、
排出管に排液が溜まつて一定量を越えると自動的に弁体
が開いて外部に排出されるようになる。そして、上記弁
体が開いているときに、排出管の下端部がU字形に形成
されているため、このU字形部分の端部の開口する排出
口から気泡が流入しない。したがつて、従来例(特開昭
55−64200号公報に示す装置)では必要であつた管理
を、この発明の装置ではする必要がなくなる。そのう
え、この発明の液体の汲み揚げ装置を酸素供給装置とし
ても使用することができる。すなわち、この発明の装置
によつて同一槽の液体を循環させる(このとき、循環す
る液体には新鮮な大気が流入する)ことにより、極めて
効果的なエアレーシヨンが行われるものであり、このエ
アレーション効果を、酸欠状態にある河川や堀池等の曝
気に活用することで、この発明の装置を環境技術に役立
てることが可能になる。That is, in the liquid pumping-up device of the present invention, a pumping pipe is arranged from a sealed vacuum chamber discharged above the liquid surface toward the liquid surface, and a vacuum chamber inside the vacuum chamber is provided on the ceiling side of the vacuum chamber. A decompression means for decompressing the inside of the vacuum chamber by sucking air is connected. Then, by decompressing the inside of the vacuum chamber using a decompression means, a liquid column due to the atmospheric pressure and its differential pressure is created in the pumping pipe, and at the lower end of this liquid column, the atmosphere is at the lower end of the pumping pipe. Alternatively, the liquid is pumped into the vacuum chamber by allowing the liquid to flow naturally through the lower end opening. As described above, in the present invention, the atmosphere is allowed to naturally flow into the liquid column in the pumping pipe from the lower end portion or the lower end opening of the pumping pipe, so that a conventional example (apparatus shown in JP-A-62-195498) In addition, the air compressor and the delivery line, which were required in the above, are not required, the apparatus becomes inexpensive, the structure thereof is simplified, and the entire apparatus is downsized. Moreover, the lower end opening of the pumping pipe is opened in the vicinity of the liquid surface, and a plate-like body is attached to the lower end portion of the pumping pipe with a predetermined distance from the lower end opening to attach the plate-like body. Since it is arranged at a position slightly submerged in the liquid from the liquid surface, the liquid vigorously flows into the dish from the outer peripheral part of the dish, and the floating matter floating on the liquid surface with this inflow is also dish-shaped. Flows into the body. Therefore, the liquid and suspended matter that have flowed into the dish can be efficiently pumped from the lower end opening of the pumping pipe that opens near the liquid surface. Further, a discharge pipe for discharging the liquid pumped up into the vacuum chamber to the outside is extended downward from the bottom of the vacuum chamber, the lower end portion of the discharge pipe is formed in a U shape, and the end portion of the U shape portion is opened. A valve element is attached to the discharge port that can be opened when the pressure at the discharge port is higher than atmospheric pressure to discharge the liquid in the discharge pipe to the outside. The vacuum chamber is closed and the vacuum chamber is sealed.
When the drainage liquid accumulates in the drainage pipe and exceeds a certain amount, the valve body automatically opens and is discharged to the outside. When the valve body is open, the lower end portion of the discharge pipe is formed in a U shape, so that bubbles do not flow from the discharge opening that opens at the end portion of the U shape portion. Therefore, the conventional example (Japanese Patent Laid-Open No.
It is no longer necessary to perform the management in the device of the present invention, which was necessary in the device shown in the 55-64200 publication). Moreover, the liquid pumping apparatus of the present invention can be used as an oxygen supply apparatus. That is, by circulating the liquid in the same tank (at this time, fresh air flows into the circulating liquid) by the device of the present invention, extremely effective aeration is performed. It is possible to utilize the device of the present invention for environmental technology by utilizing the aeration of a river or a moat which is in an oxygen-deficient state.
つぎに、この発明を実施例にもとづいて詳しく説明す
る。Next, the present invention will be described in detail based on examples.
第1図はこの発明に用いる液体の汲み揚げ装置の一実施
例を示している。図において、10は水面の上方(液面か
ら2800mm上方の位置)から下方に延びている管径25mmの
汲み揚げ管である。この汲み揚げ管10の上端部は曲成さ
れ、その上端吐出口が密封箱状の真空室11内で水平方向
を向いた状態に開口している。これにより、吐出流速に
より上記上端吐出口から吐出される水が後述する真空ポ
ンプ13に吸引されることを防いでいる。また、上記汲み
揚げ管10の下端部には密封箱状の空気室(大気導入室)
18が設けられ、この空気室18に大気を自然流入させる空
気導入管18aが接続されている。25は上記空気室18内に
流入する空気量を調節するバルブであり、上記空気導入
管18aの先端に取り付けられている。上記汲み揚げ管10
の下端には所定間隔を保つて受け皿(皿状体)24が取り
付けられている。FIG. 1 shows an embodiment of a liquid pumping apparatus used in the present invention. In the figure, 10 is a pumping pipe having a pipe diameter of 25 mm and extending downward from above the water surface (at a position 2800 mm above the liquid surface). The upper end of the scooping pipe 10 is bent, and its upper discharge port is opened in the sealed box-shaped vacuum chamber 11 so as to face the horizontal direction. This prevents water discharged from the upper-end discharge port from being sucked into the vacuum pump 13 described later due to the discharge flow velocity. A sealed box-shaped air chamber (atmosphere introduction chamber) is provided at the lower end of the pumping pipe 10.
18 is provided, and an air introducing pipe 18a for allowing atmospheric air to naturally flow into the air chamber 18 is connected. Reference numeral 25 is a valve that adjusts the amount of air flowing into the air chamber 18, and is attached to the tip of the air introducing pipe 18a. The above-mentioned pumping pipe 10
A saucer (dish-shaped body) 24 is attached to the lower end of the tray at a predetermined interval.
12は上記真空室11の上端側から外部に延びる配管であ
り、13はこの配管12の先端に接続された真空ポンプ(吸
込仕事率,110W、真空度,709水柱mm、風量,0.95m3毎分の
能力の家庭用掃除機を使用)である。また、14は上記配
管12に設けられた通気性のミストセパレーターであり、
このミストセパレーター14、真空ポンプ13で真空室11内
を減圧する際、配管12中を流れる空気から水分等を除去
し、真空ポンプ13内に水分が入り込むことを防止する。12 is a pipe extending from the upper end of the vacuum chamber 11 to the outside, and 13 is a vacuum pump connected to the end of the pipe 12 (suction work rate, 110 W, vacuum degree, 709 water column mm, air volume, 0.95 m 3 per Use a household vacuum cleaner with the capacity of minutes). Further, 14 is a breathable mist separator provided in the pipe 12,
When the inside of the vacuum chamber 11 is decompressed by the mist separator 14 and the vacuum pump 13, moisture or the like is removed from the air flowing through the pipe 12 to prevent the moisture from entering the vacuum pump 13.
15は上記真空室11の底部から垂設されている排出管であ
り、下部側でU字形トラツプ15aを形成し、先端の排出
口には逆止弁16が設けられている。この逆止弁16と上記
真空室11の底部との間の鉛直高さが真空室11内に造成す
る真空度に等しい液柱の高さ以上になるようにしてい
る。したがつて、逆止弁16は、排出管15内を流下する液
の管内液柱が真空室11内の真空度と等しくなるまでは外
部の大気圧が大きいため閉じており、大気は流入しな
い。流下する液が排出量15内に溜まつて排出管15内の液
柱が真空室11内の真空度と等しくなると排出口の内外の
圧力がバランスし、液柱がそれ以上になると逆止弁16が
開いて排出口から液が排出される。その際、排出管15内
に流入しようとする大気の流れは、U字形トラツプ15a
によつて遮断される。Reference numeral 15 is a discharge pipe vertically provided from the bottom of the vacuum chamber 11, which forms a U-shaped trap 15a on the lower side, and a check valve 16 is provided at the discharge port at the tip. The vertical height between the check valve 16 and the bottom of the vacuum chamber 11 is set to be equal to or higher than the height of the liquid column equal to the degree of vacuum created in the vacuum chamber 11. Therefore, the check valve 16 is closed because the external atmospheric pressure is large until the liquid column in the liquid flowing down in the discharge pipe 15 becomes equal to the vacuum degree in the vacuum chamber 11, and the atmosphere does not flow in. . When the liquid flowing down is accumulated in the discharge amount 15 and the liquid column in the discharge pipe 15 becomes equal to the vacuum degree in the vacuum chamber 11, the pressure inside and outside the discharge port is balanced, and when the liquid column becomes higher than that, the check valve 16 opens and the liquid is discharged from the discharge port. At that time, the flow of the atmospheric air flowing into the discharge pipe 15 is the U-shaped trap 15a.
Will be shut off.
この構成において、まず、真空ポンプ13を作動させる。
その結果、真空室11内が減圧されその内部の気圧が低下
し汲み揚げ管10内に水柱が形成されるとともに空気室18
内に大気が自然流入され、汲み揚げ管10内に激しい気液
混合の上昇流が生じ、液面付近の水がこれに受かぶ浮遊
物と一緒に上記受け皿24と空気箱18の間から吸い揚げら
れる。ついで、真空室11内に汲み揚げられた水等は排出
管15を通つて流下し、排出口に設けた逆止弁16が自動的
に開閉し、真空室11内から流下してくる水等を外部に排
出する。すなわち、排出管15内の液面位置が、逆止弁16
の位置よりも一定の高さだけ高い場合に逆止弁16を閉成
する力は0になり、上記一定の高さよりも上記液面位置
が高くなると、逆止弁16が開成し、水等の排出が始ま
り、低くなると逆止弁16が閉成する。このため、排出管
15を流下する水等の液面位置が、常に一定の高さを維持
した状態で、断続的に水等の排出が行われる。上記実施
例においては、この一定高さが略800mmであつた。ま
た、真空室11から真空ポンプ13により吸引される空気
は、ミストセパレーター14でほこりや水蒸気等の不純物
を排除されたのち、真空ポンプ13に吸い込まれる。In this structure, first, the vacuum pump 13 is operated.
As a result, the inside of the vacuum chamber 11 is decompressed, the air pressure inside the vacuum chamber 11 drops, and a water column is formed in the pumping pipe 10 and the air chamber 18
The air naturally flows into the pumping pipe 10, and a violent upflow of gas-liquid mixture occurs in the pumping pipe 10, and the water near the liquid surface sucks from between the tray 24 and the air box 18 together with the suspended matter that it receives. Fried. Then, the water or the like pumped into the vacuum chamber 11 flows down through the discharge pipe 15, the check valve 16 provided at the discharge port automatically opens and closes, and the water, etc. flowing down from the vacuum chamber 11 Is discharged to the outside. That is, the liquid level in the discharge pipe 15 is changed to the check valve 16
When the liquid level is higher than the constant height, the force to close the check valve 16 becomes 0 when the height is higher than the constant height. Is started to be discharged, and the check valve 16 is closed when the discharge becomes low. For this reason, the discharge pipe
Water and the like flowing down 15 are intermittently discharged while the liquid level is always maintained at a constant height. In the above embodiment, this constant height was approximately 800 mm. The air sucked from the vacuum chamber 11 by the vacuum pump 13 is sucked into the vacuum pump 13 after impurities such as dust and water vapor are removed by the mist separator 14.
このように、この液体の汲み揚げ装置は、汲み揚げ管10
に設けた空気室18から自然導入される空気を、汲み揚げ
管10内の水等に混合しその平均比重を小さくすることに
より汲み揚げ管10での液面高さを高くすることに加え
て、真空ポンプ13により減圧状態にされた真空室11に、
汲み揚げ管10の上部側と下部側との気圧差を利用して上
記水等を吸い上げるようになつているため、揚水の上限
を高くできる。また、汲み揚げる固形物の大きさを大き
くできる等の揚水能力を大幅に向上することができる。
しかも、従来例では必要であつた空気圧縮機や送出ライ
ンを省略することができるため、安価になるうえ、構造
が簡単化し、コンパクトにもなる。さらに、配管12にミ
ストセパレーター14を設けているため、真空ポンプ13内
に空気以外の不純物が侵入しその不純物の侵入により真
空ポンプ13が損傷されるという事態を回避することがで
きる。In this way, this liquid pumping device is equipped with a pumping pipe 10
In addition to increasing the liquid level in the scooping pipe 10 by mixing the air naturally introduced from the air chamber 18 provided in the scooping pipe 10 with water in the scooping pipe 10 to reduce its average specific gravity. , In the vacuum chamber 11 depressurized by the vacuum pump 13,
Since the water or the like is sucked up by utilizing the pressure difference between the upper side and the lower side of the pumping pipe 10, the upper limit of the pumped water can be increased. In addition, the pumping capacity such as increasing the size of the solid material to be pumped up can be greatly improved.
Moreover, since the air compressor and the delivery line, which are required in the conventional example, can be omitted, the cost is low, and the structure is simple and compact. Furthermore, since the pipe 12 is provided with the mist separator 14, it is possible to avoid a situation in which impurities other than air enter the vacuum pump 13 and the vacuum pump 13 is damaged by the intrusion of the impurities.
第2図は他の実施例に用いる液体の汲み揚げ装置を示し
ている。この装置は、真空室11aの減圧手段として真空
ポンプを用いるのではなく、ジエツトエジエクター26を
用いている。すなわち、図において、27は壁面28を境界
として真空室11aと一体的に形成されたジエツト水回収
槽であり、その上部側空間に真空室11aの上部側から延
びるジエツト水回収用配管29が突出している。このジエ
ツト水回収用配管29は真空室11a側が大径に形成されて
いる。30はジエツト水回収槽27の天井部に設けられた空
気抜き部であり、31はジエツト水回収槽23内のジエツト
水を一定レベルに維持するためのオーバーフロー管であ
る。32はジエツト水回収槽27の底部から延びるジエツト
水循環用配管であり、他端がジエツト水噴射用のジエツ
トエジエクター26に接続されている。このジエツトエジ
エクター26からはジエツト水吐出用配管33が延設され、
その先端部33aが真空室11a内に延びている。この先端部
33aは、ジエツト水回収用配管29の開口に所定の間隔を
保つて相対峙する位置に位置決めされており、そのた
め、ジエツトエジエクター26を作動させると、ジエツト
水回収槽27,ジエツト水循環用配管32,ジエツトエジエク
ター26,ジエツト水吐出用配管33,ジエツト水回収用配管
29で形成される循環路にジエツト水が勢いよく循環し、
ジエツト水流が露呈している真空室11a内においては、
真空室11a内の空気がジエツト水に巻き込まれてジエツ
ト水回収槽27側に吸引される。その結果、真空室11a内
が減圧され、汲み揚げ管10の下部側から液体等を吸い揚
げ、この液体等を排出管15aから排出する。この際、ジ
エツト水回収槽27内に運ばれた空気は空気抜き部30から
ジエツト水回収槽27の外部へ排出され、ジエツト水回収
槽27内の液体量が一定量を越えるとオーバーフロー管31
から外部へ排出される。その他の部分については第1図
の実施例と同様である。このように構成することによ
り、真空室11a内の真空度を、さらに高度にすることが
でき揚水能力をさらに向上できる。また、ジエツト水流
が、下方から上方に向かうのではなく、水平方向に向か
うため、動力が少なくてすむ。FIG. 2 shows a liquid pumping apparatus used in another embodiment. This device does not use a vacuum pump as a decompression means for the vacuum chamber 11a, but uses a jet ejector 26. That is, in the figure, 27 is a jet water recovery tank integrally formed with the vacuum chamber 11a with a wall surface 28 as a boundary, and a jet water recovery pipe 29 extending from the upper side of the vacuum chamber 11a projects into the upper space thereof. ing. The jet water recovery pipe 29 has a large diameter on the vacuum chamber 11a side. Reference numeral 30 is an air vent provided on the ceiling of the jet water recovery tank 27, and 31 is an overflow pipe for maintaining the jet water in the jet water recovery tank 23 at a constant level. Reference numeral 32 is a jet water circulation pipe extending from the bottom of the jet water recovery tank 27, and the other end thereof is connected to the jet water ejector 26 for jetting water. From this jet ejector 26, a jet water discharge pipe 33 is extended,
Its tip 33a extends into the vacuum chamber 11a. This tip
33a is positioned at the position of the opening of the jet water recovery pipe 29, which is kept at a predetermined interval and in a relative position, and therefore, when the jet ejector 26 is operated, the jet water recovery tank 27, the jet water circulation pipe 32, Jet Ejector 26, Jet Water Discharge Pipe 33, Jet Water Recovery Pipe
Jet water vigorously circulates in the circulation path formed at 29,
In the vacuum chamber 11a where the jet water flow is exposed,
The air in the vacuum chamber 11a is caught in the jet water and sucked into the jet water recovery tank 27 side. As a result, the inside of the vacuum chamber 11a is decompressed, the liquid or the like is sucked from the lower side of the scooping pipe 10, and the liquid or the like is discharged from the discharge pipe 15a. At this time, the air carried into the jet water recovery tank 27 is discharged from the air vent 30 to the outside of the jet water recovery tank 27, and when the liquid amount in the jet water recovery tank 27 exceeds a certain amount, the overflow pipe 31
Is discharged from the outside. Other parts are the same as those in the embodiment of FIG. With this configuration, the degree of vacuum in the vacuum chamber 11a can be further increased and the pumping capacity can be further improved. In addition, the jet water flow is not in the upward direction but in the horizontal direction, and therefore the power is small.
以上のように、この発明の液体の汲み揚げ装置によれ
ば、従来例(特開昭62−195498号公報に示す装置)では
必要であつた空気圧縮機、および送出ラインが必要でな
くなり、装置が安価になり、その構造が簡単化するう
え、装置全体が小形化するようになる。しかも、汲み揚
げ管の下端開口を液面近傍に開口するとともに、この下
端開口との間に所定間隔をあけた状態で上記汲み揚げ管
の下端部に皿状体を取付けてこの皿状体を液面よりやや
液中に入つた位置に配設しているため、上記皿状体の外
周部から皿状体内に液体が勢いよく流入し、この流入に
伴い、液面に浮かぶ浮遊物も皿状体内に流入する。した
がつて、上記皿状体内に流入した液体および浮遊物を、
液面近傍に開口する汲み揚げ管の下端開口から効率よく
汲み揚げることができるようになる。さらに、真空室内
に汲み揚げられた液体を外部に排出する排出管を真空室
の底部から下方に延ばし、上記排出管の下端部をU字形
に形成し、このU字形部分の端部に開口する排出口に、
この排出口での圧力が大気圧以上になつた状態で開いて
排出管の液体を外部に排出しうる弁体を取付けているた
め、真空室内を減圧すると弁体が排出口を閉じて真空室
内が密封状態になり、また、排出管に排液が溜まつて一
定量を越えると自動的に弁体が開いて外部に排出される
ようになる。そして、上記弁体が開いているときに排出
管の下端部がU字形に形成されているため、このU字形
部分の端部に開口する排出口から気泡が流入しない。し
たがつて、従来例(特開昭55−64200号公報に示す装
置)では必要であつた管理を、この発明の装置ではする
必要がなくなる。そのうえ、この発明の液体の汲み揚げ
装置を酸素供給装置としても使用することができる。す
なわち、この発明の装置によつて同一槽の液体を循環さ
せる(このとき、循環する液体には新鮮な大気が流入す
る)ことにより、極めて効果的なエアレーシヨンが行わ
れるものであり、このエアレーシヨン効果を、酸欠状態
にある河川や堀池等の曝気に活用することで、この発明
の装置を環境技術に役立てることが可能になる。As described above, according to the liquid pumping apparatus of the present invention, the air compressor and the delivery line, which are required in the conventional example (the apparatus shown in Japanese Patent Laid-Open No. 62-195498), are not necessary, and the apparatus Becomes cheaper, the structure is simplified, and the entire device becomes smaller. Moreover, the lower end opening of the pumping pipe is opened in the vicinity of the liquid surface, and a plate-like body is attached to the lower end portion of the pumping pipe with a predetermined distance from the lower end opening to attach the plate-like body. Since it is arranged at a position slightly submerged in the liquid from the liquid surface, the liquid vigorously flows from the outer peripheral portion of the dish-shaped body into the dish-shaped body, and with this inflow, suspended matter floating on the liquid surface is also dished. Inflow into the state. Therefore, the liquid and suspended matter that flowed into the dish,
It is possible to efficiently pump up from the lower end opening of the pumping pipe that opens near the liquid surface. Further, a discharge pipe for discharging the liquid pumped up into the vacuum chamber to the outside is extended downward from the bottom of the vacuum chamber, the lower end portion of the discharge pipe is formed in a U shape, and the end portion of the U shape portion is opened. At the outlet,
Since a valve element is installed that opens when the pressure at the discharge port is higher than atmospheric pressure and can discharge the liquid in the discharge pipe to the outside, when the pressure in the vacuum chamber is reduced, the valve body closes the discharge port and the vacuum chamber is closed. Becomes a sealed state, and when the drainage liquid is accumulated in the drainage pipe and exceeds a certain amount, the valve body is automatically opened and drained to the outside. Further, since the lower end portion of the discharge pipe is formed in a U shape when the valve body is opened, air bubbles do not flow from the discharge port opened at the end portion of the U shape portion. Therefore, the management of the conventional example (the apparatus disclosed in Japanese Patent Laid-Open No. 55-64200) is no longer necessary in the apparatus of the present invention. Moreover, the liquid pumping apparatus of the present invention can be used as an oxygen supply apparatus. That is, by circulating the liquid in the same tank (at this time, fresh air flows into the circulating liquid) by the device of the present invention, extremely effective air race is performed. It is possible to utilize the device of the present invention for environmental technology by utilizing the aeration of a river or a moat which is in an oxygen-deficient state.
第1図はこの発明の一実施例の断面図、第2図は他の実
施例の要部断面図である。 10……汲み揚げ管、11……真空室、13……真空ポンプ、
15……排出管FIG. 1 is a sectional view of an embodiment of the present invention, and FIG. 2 is a sectional view of a main portion of another embodiment. 10 …… pumping pipe, 11 …… vacuum chamber, 13 …… vacuum pump,
15 ... Discharge pipe
Claims (1)
液面に向けて汲み揚げ管を配設し、上記真空室の天井部
側に、真空室内の空気を吸引することにより上記真空室
内を減圧する減圧手段を接続した液体の汲み揚げ装置で
あつて、上記汲み揚げ管の下端開口を液面近傍に開口す
るとともに、この下端開口との間に所定間隔をあけた状
態で上記汲み揚げ管の下端部に皿状体を取付けてこの皿
状体を液面よりやや液中に入つた位置に配設し、上記真
空室内を減圧手段で減圧することにより、大気圧との差
圧による液柱を汲み揚げ管内に作るとともに、この液柱
の下端部に上記汲み揚げ管の下端部もしくは下端開口か
ら大気を自然流入させて上記真空室内に液体を汲み揚
げ、この真空室内に汲み揚げられた液体を外部に排出す
る排出管を真空室の底部から下方に延ばし、上記排出管
の下端部をU字形に形成し、このU字形部分の端部に開
口する排出口に、この排出口での圧力が大気圧以上にな
つた状態で開いて排出管の液体を外部に排出しうる弁体
を取付けたことを特徴とする液体の汲み揚げ装置。1. A pumping pipe is provided from a hermetically sealed vacuum chamber disposed above the liquid surface toward the liquid surface, and air in the vacuum chamber is sucked to the ceiling side of the vacuum chamber. A pumping device for a liquid connected to a decompression means for decompressing the inside of the vacuum chamber, wherein the lower end opening of the pumping pipe is opened near the liquid surface, and a predetermined interval is provided between the lower end opening and the lower end opening. A dish-shaped body is attached to the lower end of the pumping pipe, and the dish-shaped body is arranged at a position slightly immersed in the liquid from the liquid surface. A liquid column due to the differential pressure is created in the pumping pipe, and at the lower end of the liquid column, the atmosphere is allowed to naturally flow into the vacuum chamber from the lower end or the lower end opening of the pumping pipe, and the liquid is pumped into the vacuum chamber. The discharge pipe for discharging the pumped liquid to the outside is installed in the vacuum chamber. The lower end of the discharge pipe is formed in a U shape, and is opened at the discharge port opening at the end of the U-shaped portion while the pressure at the discharge port is equal to or higher than atmospheric pressure. A liquid pumping apparatus, which is equipped with a valve body capable of discharging liquid in a discharge pipe to the outside.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP63029921A JPH0786360B2 (en) | 1988-02-10 | 1988-02-10 | Liquid pumping equipment |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP63029921A JPH0786360B2 (en) | 1988-02-10 | 1988-02-10 | Liquid pumping equipment |
Related Child Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP4138610A Division JP2781306B2 (en) | 1992-05-29 | 1992-05-29 | Method for pumping liquid and apparatus used therefor |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH01208600A JPH01208600A (en) | 1989-08-22 |
JPH0786360B2 true JPH0786360B2 (en) | 1995-09-20 |
Family
ID=12289457
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP63029921A Expired - Fee Related JPH0786360B2 (en) | 1988-02-10 | 1988-02-10 | Liquid pumping equipment |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0786360B2 (en) |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS62195498A (en) * | 1986-01-28 | 1987-08-28 | レイモンド アンソニ− ブレツクナ− | Method and device for scooping up liquid |
-
1988
- 1988-02-10 JP JP63029921A patent/JPH0786360B2/en not_active Expired - Fee Related
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS62195498A (en) * | 1986-01-28 | 1987-08-28 | レイモンド アンソニ− ブレツクナ− | Method and device for scooping up liquid |
Also Published As
Publication number | Publication date |
---|---|
JPH01208600A (en) | 1989-08-22 |
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