JPH04102600A - Liquid transferring device - Google Patents

Liquid transferring device

Info

Publication number
JPH04102600A
JPH04102600A JP21494990A JP21494990A JPH04102600A JP H04102600 A JPH04102600 A JP H04102600A JP 21494990 A JP21494990 A JP 21494990A JP 21494990 A JP21494990 A JP 21494990A JP H04102600 A JPH04102600 A JP H04102600A
Authority
JP
Japan
Prior art keywords
liquid
pressure
tank
regulating tank
pipe
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.)
Pending
Application number
JP21494990A
Other languages
Japanese (ja)
Inventor
Masashi Masuda
増田 昌士
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.)
Toshiba Corp
Itel Corp
Original Assignee
Toshiba Corp
Itel Corp
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 Toshiba Corp, Itel Corp filed Critical Toshiba Corp
Priority to JP21494990A priority Critical patent/JPH04102600A/en
Publication of JPH04102600A publication Critical patent/JPH04102600A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To greatly reduce troublesomeness in maintenance and supervising by providing an overflow pipe with its opening provided to a specified height of the liquid level, in a pressure-regulating tank, and by providing a drain pipe which guides the liquid overflowing the overflow pipe to a receiving tank. CONSTITUTION:With a vacuum pump 10 started with a three-way valve 11 driven and a pressure-regulating tank 4 communicated with the vacuum pump 10, liquid 2 in a liquid storage tank 1 is sucked up at a fixed flow rate through a suction pipe 6, and is stored in the pressure-regulating tank 4. The liquid sucked up to the pressure- regulating tank 4 and stored therein flows over the upper edge of an overflow pipe 7 and runs down the inside of a drain pipe 8 and is delivered toward a receiving tank 3. The delivery is made in natural running-down by head pressure corresponding to the difference H4+H3 between the upper edge of the overflow pipe 7 provided in the pressure-regulating tank 4 and the level of the liquid in the receiving tank 3. The height (h) to the level of the liquid in the liquid storage tank 1 is detected with a transmitter-equipped liquid level measuring instrument 13. When the level of the liquid comes near to the lower end of the suction pipe 6, the three-way valve 11 is communicated with the atmosphere side by operation of an adjuster 14, and thereby the inside of the pressure-regulating tank 4 is released from depressurized state and transfer of the liquid is stopped.

Description

【発明の詳細な説明】 〔発明の目的〕 (産業上の利用分野) 本発明は液体移送装置に係り、特に一定流量で液体を移
送することが可能であり、また接液部に流量測定装置、
ポンプや流量調節弁などの可動機器を設けることなく、
装置構成が簡素で保守管理が極めて容易な液体移送装置
に関する。
[Detailed Description of the Invention] [Object of the Invention] (Industrial Application Field) The present invention relates to a liquid transfer device, and in particular, it is capable of transferring a liquid at a constant flow rate, and a flow rate measuring device is provided in the wetted part. ,
No need for moving equipment such as pumps or flow control valves.
The present invention relates to a liquid transfer device that has a simple device configuration and is extremely easy to maintain and manage.

(従来の技術) 化学工場や原子力関連施設から排出される廃液には毒性
、腐食性が高いものが多く、その処理を実施するに際し
ては移送取扱いに充分に注意する必要がある。特に原子
力関連施設から排出される放射性廃液等については、放
射線被曝を可及的に低減する必要があり、廃液処理装置
は一般の作業区域から隔離された管理区域に設置され、
かつ保守管理作業を容易に実施することが困難な場所に
設置される場合が多い。
(Prior Art) Many waste liquids discharged from chemical factories and nuclear power-related facilities are highly toxic and corrosive, and when processing them, it is necessary to be careful in handling the transfer. In particular, it is necessary to reduce radiation exposure as much as possible with respect to radioactive liquid waste discharged from nuclear-related facilities, and waste liquid treatment equipment is installed in a controlled area separated from general work areas.
In addition, they are often installed in locations where it is difficult to easily carry out maintenance and management work.

このような廃液処理装置において、処理操作の定常性を
維持するために液体を一定流量で移送する移送装置が必
要であり、従来、この種の移送装置は、通常の化学プラ
ントの場合と同様に、液体を流通させる配管系内に流量
測定装置、ポンプや流量調節弁などの可動機器を配設し
て構成されている。
Such waste liquid treatment equipment requires a transfer device that transfers the liquid at a constant flow rate in order to maintain the stability of treatment operations. It is constructed by disposing movable devices such as a flow rate measuring device, a pump, and a flow rate regulating valve within a piping system that circulates liquid.

(発明が解決しようとする課題) しかしながら、従来の移送装置においては腐食性や毒性
が高い液体に直接的にポンプや流量調節弁等の可動機器
が接触するため、可動部品の腐食損傷や性能劣化が進行
し易く、定期的に装置を停止して保守点検や部品交換を
行なう必要があり、保守作業に多大な労力と時間とを要
する欠点があった。
(Problem to be solved by the invention) However, in conventional transfer devices, movable equipment such as pumps and flow control valves come into direct contact with highly corrosive and toxic liquids, resulting in corrosion damage to movable parts and performance deterioration. However, it is necessary to periodically stop the device for maintenance inspection and parts replacement, which has the disadvantage that maintenance work requires a great deal of effort and time.

特に放射性廃液を取扱う移送装置においては作業員の放
射線被曝が増大し、廃液に直接接触する危険性も高く、
何らかの対策が望まれていた。
In particular, in transfer equipment that handles radioactive waste liquid, the radiation exposure of workers increases and the risk of direct contact with the waste liquid is high.
Some kind of countermeasure was desired.

本発明は上記の問題点を解決するためになされたもので
あり、接液部に可動部を有する機器を使用せずに装置の
構成を簡素化し、保守管理作業を大幅に低減することが
可能であり、また一定流量で液体を移送することが可能
な液体移送装置を提供することを目的とする。
The present invention has been made to solve the above-mentioned problems, and it is possible to simplify the configuration of the device without using equipment with moving parts in wetted parts, and to significantly reduce maintenance work. Another object of the present invention is to provide a liquid transfer device capable of transferring liquid at a constant flow rate.

〔発明の構成〕[Structure of the invention]

(課題を解決するための手段) 上記目的を達成するため本発明は液体貯槽に貯留した液
体を受槽に移送する液体移送装置において、液体貯槽お
よび受槽より高所に圧力調整槽を配設し、この圧力調整
槽の内部圧力を所定値に調整する減圧装置を装備し、圧
力調整槽内の減圧により液体貯槽内の液体を吸い上げる
吸上げ管の上端を上記圧力調整槽の底部に接続する一方
、上記圧力調整槽内の所定液面高さに開口を有する溢流
管を設け、溢流管から溢流する液体を受槽に案内する排
出管を配設したことを特徴とする。
(Means for Solving the Problems) In order to achieve the above object, the present invention provides a liquid transfer device for transferring liquid stored in a liquid storage tank to a receiving tank, in which a pressure regulating tank is disposed at a higher location than the liquid storage tank and the receiving tank, Equipped with a pressure reducing device that adjusts the internal pressure of this pressure regulating tank to a predetermined value, and connecting the upper end of a suction pipe that sucks up the liquid in the liquid storage tank by reducing the pressure in the pressure regulating tank to the bottom of the pressure regulating tank, The present invention is characterized in that an overflow pipe having an opening at a predetermined liquid level height in the pressure regulating tank is provided, and a discharge pipe is provided for guiding the liquid overflowing from the overflow pipe to the receiving tank.

(作用) 上記構成に係る液体移送装置において、減圧装置によっ
て圧力調整槽内が減圧され所定の圧力値に調整されるこ
とにより、液体貯槽内に貯留されていた液体が吸上げ管
を通り圧力調整槽内に吸い上げられる。吸い上げられた
液体のうち溢流管の開口より上部の液体は、溢流管から
一定流量で溢流し圧力調整槽と受槽との間のヘッド(波
頭)差によって自然流下により受槽内に移送される。
(Function) In the liquid transfer device having the above configuration, the pressure inside the pressure adjustment tank is reduced by the pressure reducing device and adjusted to a predetermined pressure value, so that the liquid stored in the liquid storage tank passes through the suction pipe and the pressure is adjusted. It is sucked up into the tank. Of the liquid sucked up, the liquid above the opening of the overflow pipe overflows from the overflow pipe at a constant flow rate and is transferred to the receiving tank by gravity due to the head difference between the pressure adjustment tank and the receiving tank. Ru.

このように本発明に係る液体移送装置によれば、液体の
移送経路の接液部に流量測定装置、ポンプや流量調節弁
等の可動機器を配設ゼずに、圧力調整槽内の圧力調整に
よって液体を一定流量で移送することができる。また接
液部に可動機器を配設していないため、従来装置のよう
な可動部の損傷や劣化が起こらず、装置の保守点検が容
易であり、長期間に渡って装置を連続的に運転すること
ができる。
As described above, according to the liquid transfer device according to the present invention, the pressure in the pressure adjustment tank can be adjusted without installing movable devices such as a flow rate measurement device, a pump, or a flow rate control valve in the liquid contact portion of the liquid transfer path. The liquid can be transferred at a constant flow rate. In addition, because there are no movable devices in the wetted parts, there is no damage or deterioration of moving parts like in conventional equipment, and maintenance and inspection of the equipment is easy, allowing continuous operation of the equipment over long periods of time. can do.

特に放射性液体を取扱う装置においては、保守点検時間
の短縮化に伴い、保守作業員の放射線被曝を大幅に低減
することができる。
Particularly in equipment that handles radioactive liquids, the radiation exposure of maintenance workers can be significantly reduced as maintenance and inspection time is shortened.

(実施例) 次に本発明の一実施例について添付図面を参照して説明
する。第1図は本発明に係る液体移送装置の一実施例を
示す断面図である。
(Example) Next, an example of the present invention will be described with reference to the accompanying drawings. FIG. 1 is a sectional view showing an embodiment of a liquid transfer device according to the present invention.

すなわち本実施例に係る液体移送装置は、液体貯槽1に
貯留した液体2を受槽3に移送する液体移送装置におい
て、液体貯槽]および受槽3より高所に圧力調整槽4を
配設し、この圧力調整槽4の内部圧力P1を所定値に調
整する減圧装置5を装備し、圧力調整槽4内の減圧によ
り液体貯槽1内の液体2を吸い上げる吸上げ管6の上端
を上記圧力調整槽4の底部に接続する一方、上記圧力調
整槽4内の所定液面高さに開口を有する溢流管7を設け
、溢流管7から溢流する液体2を受槽3に案内する排出
管8を配設して構成される。
That is, the liquid transfer device according to this embodiment is a liquid transfer device that transfers liquid 2 stored in a liquid storage tank 1 to a receiving tank 3, in which a pressure regulating tank 4 is arranged at a higher location than the liquid storage tank and the receiving tank 3, and A pressure reducing device 5 is installed to adjust the internal pressure P1 of the pressure regulating tank 4 to a predetermined value. An overflow pipe 7 is connected to the bottom of the pressure regulating tank 4 and has an opening at a predetermined liquid level height in the pressure regulating tank 4, and a discharge pipe 8 is provided to guide the liquid 2 overflowing from the overflow pipe 7 to the receiving tank 3. Arranged and configured.

また減圧装置5は、圧力調整槽4内の気相部を減圧配管
9を経由して排気する真空ポンプ10と、減圧配管9に
介装され、圧力調整槽4内の気体の流路を閉止したり、
大気側または真空ポンプ10側に切換える三方弁11と
、圧力調整槽4内と液体貯槽1内との差圧(P 2  
P + )を検出する差圧発信器12と、液体貯槽1内
の液面を検出する発信器付き液面計13と、発信器付き
液面計13からの液面検出信号および差圧発信器12か
らの差圧信号を入力し、圧力調整槽4内の圧力P1を所
定値に制御するために三方弁11を駆動する駆動信号を
出力する調節器14とから構成される。
Further, the pressure reducing device 5 is interposed in the pressure reducing pipe 9 and a vacuum pump 10 that exhausts the gas phase part in the pressure regulating tank 4 via the pressure reducing pipe 9, and is installed in the pressure reducing pipe 9 to close the flow path of the gas in the pressure regulating tank 4. or
The three-way valve 11 that switches to the atmosphere side or the vacuum pump 10 side and the differential pressure between the pressure adjustment tank 4 and the liquid storage tank 1 (P 2
A differential pressure transmitter 12 that detects P + ), a liquid level gauge 13 with a transmitter that detects the liquid level in the liquid storage tank 1, and a liquid level detection signal from the liquid level gauge 13 with a transmitter and a differential pressure transmitter. 12, and a regulator 14 which outputs a drive signal to drive the three-way valve 11 in order to control the pressure P1 in the pressure regulating tank 4 to a predetermined value.

また圧力調整槽4と受槽3とを接続する排出管8の下端
は、受槽3の底部に形成されたピット状の凹部15内に
浸漬される。受槽3内の液体がほぼ全量排出された場合
においても、凹部15内には排出管8内を満たすに充分
な量の液体が残留するように構成されている。
Further, the lower end of the discharge pipe 8 connecting the pressure regulating tank 4 and the receiving tank 3 is immersed in a pit-shaped recess 15 formed at the bottom of the receiving tank 3. Even when almost all of the liquid in the receiving tank 3 is discharged, a sufficient amount of liquid remains in the recess 15 to fill the discharge pipe 8.

さらに排出管8の内径は、吸上げ管6より大きく設定し
であるため、排出管8内に沈殿物などが付着した場合に
おいても、流下する液体の流量が変化するおそれは少な
い。
Further, since the inner diameter of the discharge pipe 8 is set to be larger than that of the suction pipe 6, even if deposits or the like adhere to the inside of the discharge pipe 8, there is little possibility that the flow rate of the flowing liquid will change.

吸上げ管6の内表面には耐食性および耐摩耗性に優れた
SUS材などを張設し、内表面の腐食等による粗面化を
防止し、流路断面積および流量係数の変動を防止すると
よい。
The inner surface of the suction pipe 6 is lined with a material such as SUS, which has excellent corrosion resistance and wear resistance, to prevent the inner surface from becoming rough due to corrosion, etc., and to prevent fluctuations in the flow path cross-sectional area and flow coefficient. good.

また真空ポンプ10による圧力調製槽4内の減圧時に、
排出管8を通り受槽3側から圧力調整槽4側に液体が逆
流することを防止するため、排出管8の高さ(H3+H
4)は吸上げ管6における揚程H,より大きく設定して
いる。
Furthermore, when the pressure inside the pressure adjustment tank 4 is reduced by the vacuum pump 10,
In order to prevent liquid from flowing back through the discharge pipe 8 from the receiving tank 3 side to the pressure adjustment tank 4 side, the height of the discharge pipe 8 (H3 + H
4) is set larger than the lift height H in the suction pipe 6.

液体貯槽1内の液体2を受槽3に移送する場合は、まず
、圧力調整槽4内に液体2を吸い上げる工程を行なう。
When transferring the liquid 2 in the liquid storage tank 1 to the receiving tank 3, first a step of sucking up the liquid 2 into the pressure adjustment tank 4 is performed.

すなわち、三方弁11を駆動させて圧力調整槽4を真空
ポンプ10に連通させた状態で真空ポンプ10を起動す
ると、圧力調整槽4内の減圧に伴って、吸上げ管6を通
り液体貯槽1内の液体2が一定流量で吸い上げられ、圧
力調整槽4内に収容される。このとき排出管8内の液体
も圧力調整槽4側に逆流するように吸引されるが排出管
8の高さ(H3+H4)が吸上げ管6の揚程H1よりも
大きいため、受槽3側から圧力調製槽4側に液体が連続
的に逆流することはなく、圧力調整槽4内の減圧度に応
じた液頭圧を生じた時点で均衡する。また受槽3の凹部
15内に貯留されていた液体が排出管8内を充分に満た
すため、排出管8における水封切れを生じるおそれもな
い。
That is, when the vacuum pump 10 is started with the three-way valve 11 being driven to communicate the pressure adjustment tank 4 with the vacuum pump 10, as the pressure inside the pressure adjustment tank 4 is reduced, the liquid flows through the suction pipe 6 and into the liquid storage tank 1. The liquid 2 inside is sucked up at a constant flow rate and stored in the pressure regulating tank 4. At this time, the liquid in the discharge pipe 8 is also sucked back to the pressure regulating tank 4 side, but since the height of the discharge pipe 8 (H3 + H4) is greater than the lift height H1 of the suction pipe 6, the pressure is increased from the receiving tank 3 side. The liquid does not continuously flow back to the adjustment tank 4 side, and is balanced when a liquid head pressure corresponding to the degree of pressure reduction in the pressure adjustment tank 4 is generated. Further, since the liquid stored in the recess 15 of the receiving tank 3 sufficiently fills the discharge pipe 8, there is no fear that the water seal in the discharge pipe 8 will break.

すなわち圧力調整槽4内の圧力をPiまで減圧すると、
圧力P1に相当する波頭を生じるまで排出管8内を液体
が上昇するが、この排出管8内に空気が入り込んで減圧
操作が不可能となることはない。
That is, when the pressure inside the pressure adjustment tank 4 is reduced to Pi,
Although the liquid rises in the discharge pipe 8 until a wave crest corresponding to the pressure P1 is generated, air does not enter the discharge pipe 8 and the depressurization operation becomes impossible.

圧力調整槽4内に吸い上げられ収容された液体は、溢流
管7の上縁部から一定流量で溢流し排出管8を通り、受
槽3方向に払い出される。この払出しは、圧力調整槽4
内に設けた溢流管7の上縁から受槽3内の液面高さとの
差(H4+H3)に相当するヘッド圧(液頭圧)によっ
て自然流下によりなされる。
The liquid sucked up and stored in the pressure regulating tank 4 overflows at a constant flow rate from the upper edge of the overflow pipe 7, passes through the discharge pipe 8, and is discharged in the direction of the receiving tank 3. This discharge is carried out in the pressure adjustment tank 4.
This is done by gravity due to the head pressure (liquid head pressure) corresponding to the difference (H4+H3) between the upper edge of the overflow pipe 7 provided inside and the liquid level height in the receiving tank 3 (H4+H3).

液体貯槽1−内の液面高さhは発信器付液面計13によ
って検出され、この液面高さhが吸上げ管6の下端近傍
まで降下すると、調節器14によって三方弁11が大気
側と連通ずるように回動され、圧力調整槽4内の減圧状
態が解除され、液体2の移送が停止される。
The liquid level height h in the liquid storage tank 1- is detected by the liquid level gauge 13 with a transmitter, and when the liquid level h falls to near the lower end of the suction pipe 6, the three-way valve 11 is opened to the atmosphere by the regulator 14. The pressure regulating tank 4 is rotated so as to be in communication with the side, the reduced pressure state in the pressure regulating tank 4 is released, and the transfer of the liquid 2 is stopped.

ここて排出管8における水封切れを起こすことなく、液
体貯槽1から吸上げ管6を通して液体2を圧力調整槽4
内に吸い上げるためには、圧力調整槽4内の圧力P、を
下記(1)式の範囲内に設定することが必要である。
Here, the liquid 2 is passed from the liquid storage tank 1 through the suction pipe 6 to the pressure adjustment tank 4 without causing the water seal in the discharge pipe 8 to break.
In order to siphon the water into the tank, it is necessary to set the pressure P in the pressure adjustment tank 4 within the range of equation (1) below.

P2−pH2>P、 >P3−pH3・・・・・・(]
)ここでP2は液体貯槽1の液面に作用する圧力、P3
は受槽3の液面に作用する圧力、 ρは液体の比重、 H2は液面貯槽1の底面から溢流管7の上縁までの高さ
、 H3は受槽3の液面から圧力調整槽4の底面までの高さ である。
P2-pH2>P, >P3-pH3...(]
) Here, P2 is the pressure acting on the liquid level of the liquid storage tank 1, and P3
is the pressure acting on the liquid level in the receiver tank 3, ρ is the specific gravity of the liquid, H2 is the height from the bottom of the liquid level storage tank 1 to the upper edge of the overflow pipe 7, H3 is the height from the liquid level in the receiver tank 3 to the pressure adjustment tank 4 This is the height to the bottom of the

また、圧力調整槽4内の圧力をPlに保持した状態にお
いて、吸上げ管6によって単位時間当りに吸い上げられ
る液体2の流量qは下記(2)式%式% ここでに、は吸上げ管6全体の流量係数、aは吸上げ管
6の液体通過断面積、 gは型皿加速度、 hは液体貯槽1における液体深さ である。
In addition, in a state where the pressure in the pressure adjustment tank 4 is maintained at Pl, the flow rate q of the liquid 2 sucked up per unit time by the suction pipe 6 is expressed by the following formula (2) % formula % Here, is the suction pipe 6 is the overall flow rate coefficient, a is the liquid passage cross-sectional area of the suction pipe 6, g is the mold plate acceleration, and h is the liquid depth in the liquid storage tank 1.

したがって(2)式から明らかなように(P2−P、)
−ρ(H2−h)が一定となるように制御することによ
りqは一定になり、一定流量で液体2を移送することが
できる。
Therefore, as is clear from equation (2), (P2-P,)
By controlling -ρ(H2-h) to be constant, q becomes constant, and the liquid 2 can be transferred at a constant flow rate.

ここで液体貯槽1内の圧力P2と、圧力調整槽4内の圧
力P との差(P2  PI)は差圧発信器12によっ
て検出され、その検出信号は調節器14に入力される。
Here, the difference (P2 PI) between the pressure P2 in the liquid storage tank 1 and the pressure P in the pressure adjustment tank 4 is detected by the differential pressure transmitter 12, and the detection signal is input to the regulator 14.

一方液体貯槽1から圧力調整槽4までの揚程(H2−h
)は、発信器付液面計13で検出され、その検出信号も
調節器14に入力される。
On the other hand, the lift height from the liquid storage tank 1 to the pressure adjustment tank 4 (H2-h
) is detected by the level gauge 13 with a transmitter, and the detection signal is also input to the regulator 14.

調節器14は、雨検出信号に基づいて[(P2−p  
)−ρ(H2−h)]を演算し、この値が予め定められ
た所定値となるように三方弁11を回動する制御信号を
出力し、圧力調整槽4内の圧力P1を所定値に設定する
The regulator 14 adjusts [(P2-p
)-ρ(H2-h)], outputs a control signal to rotate the three-way valve 11 so that this value becomes a predetermined value, and sets the pressure P1 in the pressure regulating tank 4 to a predetermined value. Set to .

なお排出管8内における液体2の自由落下を保証するた
めに、排出管8の液体通過断面積すは下記(3)式の範
囲に設定される。
In order to ensure free fall of the liquid 2 within the discharge pipe 8, the liquid passage cross-sectional area of the discharge pipe 8 is set within the range expressed by the following equation (3).

ここでに2は排出管8全体の流量係数、H4は圧力調整
槽4の底面から溢流管7の上縁までの高さ である。
Here, 2 is the flow coefficient of the entire discharge pipe 8, and H4 is the height from the bottom of the pressure regulating tank 4 to the upper edge of the overflow pipe 7.

また(2)式において液体貯槽1が吸上げ量に比較して
充分に大きな容量を有する大気開放槽であり、P2およ
びhの変動がないものと仮定すると、液体流量qは圧力
調整槽4内の圧力P1によって一義的に決定される。
In addition, in equation (2), assuming that the liquid storage tank 1 is an air-open tank with a sufficiently large capacity compared to the suction amount and that there is no fluctuation in P2 and h, the liquid flow rate q in the pressure adjustment tank 4 is It is uniquely determined by the pressure P1 of .

このように本実施例に係る液体移送装置によれば、圧力
調整槽4内の圧力調整を行なうことにより液体貯槽1か
ら受槽3に液体2を一定流量で移送することができる。
As described above, according to the liquid transfer device according to this embodiment, by adjusting the pressure in the pressure adjustment tank 4, the liquid 2 can be transferred from the liquid storage tank 1 to the receiving tank 3 at a constant flow rate.

特に本実施例装置においては接液部に流量測定器、ポン
プや流量調節弁などの可動機器を配備する必要がなく、
装置構成が極めて簡素化され、取扱いも容易である。し
たがって構成機器の故障がほとんどなく、装置の運転操
作および保守管理が極めて容易になり長期間に渡って連
続的に運転を継続することができる。
In particular, in the device of this embodiment, there is no need to provide movable equipment such as a flow rate measuring device, pump, or flow rate regulating valve in the wetted part.
The device configuration is extremely simplified and handling is easy. Therefore, there are almost no failures of the component equipment, and the operation and maintenance of the device is extremely easy, allowing continuous operation over a long period of time.

次に本発明の他の実施例について第2図を参照して説明
する。本実施例に係る液体移送装置は、第1図に示す構
成に加えて、圧力調整槽4上部の減圧配管9に液溜め1
6を配設するとともに、圧力調整槽4内の液面の異常上
昇を検知する超音波液面計17を圧力調整槽4上部に装
備して構成される。
Next, another embodiment of the present invention will be described with reference to FIG. In addition to the configuration shown in FIG.
6 is disposed, and an ultrasonic liquid level gauge 17 for detecting an abnormal rise in the liquid level in the pressure regulating tank 4 is installed on the top of the pressure regulating tank 4.

上記液溜め16の取付高さH3は、液体貯槽1に作用す
ると考えられる最大圧力P  が作用しl1ax た場合においても液体が上昇しないように、H5−P 
  /ρで表わされる高さよりも高い位置にff1l! 設けられる。
The mounting height H3 of the liquid reservoir 16 is set so that the liquid does not rise even when the maximum pressure P that is considered to act on the liquid storage tank 1 acts on the liquid storage tank 1.
ff1l at a position higher than the height expressed by /ρ! provided.

本実施例によれば、誤動作等によって圧力調整槽4内が
過度に減圧された場合や液体貯槽1内に過度の内圧が作
用した場合においても、減圧配管9を上昇する液体は液
溜め16において貯留される。そのため、液体が三方弁
11内に侵入して損傷を引起すことが防止される。
According to this embodiment, even if the inside of the pressure adjustment tank 4 is excessively depressurized due to a malfunction or the like or excessive internal pressure is applied inside the liquid storage tank 1, the liquid rising through the depressurization pipe 9 is kept in the liquid reservoir 16. stored. Therefore, liquid is prevented from entering the three-way valve 11 and causing damage.

また圧力調整槽4内が減圧されても液体2が圧力調整槽
4に吸い上げられない場合や、逆に圧力調整槽4内の液
面が異常に上昇して、予め設定した液面異常高(Hab
)に達した場合、それらの異常は超音波液面計17によ
って検知される。検知信号は調節器14aに送信され、
調節器は装置の作動を停止する。したがって、液面の異
常な上昇または降下による機器の損傷を未然に防止する
ことができる。
In addition, even if the pressure inside the pressure adjustment tank 4 is reduced, the liquid 2 may not be sucked up into the pressure adjustment tank 4, or conversely, the liquid level in the pressure adjustment tank 4 may rise abnormally and the liquid level may rise to a preset abnormal level ( Hab
), those abnormalities are detected by the ultrasonic liquid level gauge 17. The detection signal is sent to the regulator 14a,
The regulator deactivates the device. Therefore, damage to equipment due to abnormal rise or fall of the liquid level can be prevented.

〔発明の効果〕〔Effect of the invention〕

以上説明の通り本発明に係る液体移送装置によれば、液
体の移送経路の接液部に流量測定器、ポンプや流量調節
弁等の可動機器を配設せずに、圧力調整槽内の圧力調整
によって液体を一定流量で移送することができる。した
がって、可動部の損傷や劣化が起こらず、装置の保守点
検が容易であり、長期間に渡って装置を連続的に運転す
ることができる。
As explained above, according to the liquid transfer device according to the present invention, the pressure in the pressure regulating tank can be adjusted without disposing movable equipment such as a flow meter, a pump, or a flow control valve in the liquid contact part of the liquid transfer path. Adjustment allows liquid to be transferred at a constant flow rate. Therefore, the movable parts are not damaged or deteriorated, maintenance and inspection of the device is easy, and the device can be operated continuously over a long period of time.

特に放射性液体を取扱う装置においては、保守点検時間
の短縮化に伴い、保守作業員の放射線被曝を大幅に低減
することができる。
Particularly in equipment that handles radioactive liquids, the radiation exposure of maintenance workers can be significantly reduced as maintenance and inspection time is shortened.

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

第1図は本発明に係る液体移送装置の一実施例を示す断
面図、第2図は本発明の他の実施例を示す断面図である
。 1・・・液体貯槽、2・・・液体、3・・・受槽、4・
・・圧力調整槽、5・・・減圧装置、6・・・吸上げ管
、7・・・溢流管、8・・・排出管、9・・・減圧配管
、10・・・真空ポンプ、11・・・三方弁、12・・
・差圧発信器、13・・・発信器付液面計、14.14
a・・・調節器、15・・・凹部、16・・・液溜め、
17・・・超音波液面計。
FIG. 1 is a sectional view showing one embodiment of a liquid transfer device according to the present invention, and FIG. 2 is a sectional view showing another embodiment of the present invention. 1...Liquid storage tank, 2...Liquid, 3...Receiving tank, 4...
... Pressure adjustment tank, 5 ... Pressure reduction device, 6 ... Suction pipe, 7 ... Overflow pipe, 8 ... Discharge pipe, 9 ... Pressure reduction piping, 10 ... Vacuum pump, 11... Three-way valve, 12...
・Differential pressure transmitter, 13...Liquid level gauge with transmitter, 14.14
a...Adjuster, 15...Recess, 16...Liquid reservoir,
17...Ultrasonic liquid level gauge.

Claims (1)

【特許請求の範囲】[Claims] 液体貯槽に貯留した液体を受槽に移送する液体移送装置
において、液体貯槽および受槽より高所に圧力調整槽を
配設し、この圧力調整槽の内部圧力を所定値に調整する
減圧装置を装備し、圧力調整槽内の減圧により液体貯槽
内の液体を吸い上げる吸上げ管の上端を上記圧力調整槽
の底部に接続する一方、上記圧力調整槽内の所定液面高
さに開口を有する溢流管を設け、溢流管から溢流する液
体を受槽に案内する排出管を配設したことを特徴とする
液体移送装置。
In a liquid transfer device that transfers liquid stored in a liquid storage tank to a receiving tank, a pressure regulating tank is installed at a higher place than the liquid storage tank and the receiving tank, and a pressure reducing device is installed to adjust the internal pressure of this pressure regulating tank to a predetermined value. , an overflow pipe having an opening at a predetermined liquid level height in the pressure regulating tank, the upper end of which is connected to the bottom of the pressure regulating tank for sucking up the liquid in the liquid storage tank by reducing the pressure in the pressure regulating tank; 1. A liquid transfer device characterized in that a discharge pipe is provided for guiding the liquid overflowing from the overflow pipe to a receiving tank.
JP21494990A 1990-08-16 1990-08-16 Liquid transferring device Pending JPH04102600A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP21494990A JPH04102600A (en) 1990-08-16 1990-08-16 Liquid transferring device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP21494990A JPH04102600A (en) 1990-08-16 1990-08-16 Liquid transferring device

Publications (1)

Publication Number Publication Date
JPH04102600A true JPH04102600A (en) 1992-04-03

Family

ID=16664232

Family Applications (1)

Application Number Title Priority Date Filing Date
JP21494990A Pending JPH04102600A (en) 1990-08-16 1990-08-16 Liquid transferring device

Country Status (1)

Country Link
JP (1) JPH04102600A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101410812B1 (en) * 2012-12-18 2014-06-27 한국항공우주연구원 Pressurized Type High-Flux Fluid Delivery System
JP2015510477A (en) * 2012-02-24 2015-04-09 アドバンスト テクノロジー マテリアルズ,インコーポレイテッド System and method for delivering fluid
CN111847370A (en) * 2020-08-12 2020-10-30 中国石油化工股份有限公司 Heavy oil railway unloading system capable of prejudging completion of unloading
CN114134918A (en) * 2021-11-10 2022-03-04 上海建工四建集团有限公司 Use method of full-automatic control type vacuum deep well device

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2015510477A (en) * 2012-02-24 2015-04-09 アドバンスト テクノロジー マテリアルズ,インコーポレイテッド System and method for delivering fluid
US9695985B2 (en) 2012-02-24 2017-07-04 Entegris, Inc. Fluid delivery system and method
US10495259B2 (en) 2012-02-24 2019-12-03 Entegris, Inc. Fluid delivery system and method
KR101410812B1 (en) * 2012-12-18 2014-06-27 한국항공우주연구원 Pressurized Type High-Flux Fluid Delivery System
CN111847370A (en) * 2020-08-12 2020-10-30 中国石油化工股份有限公司 Heavy oil railway unloading system capable of prejudging completion of unloading
CN114134918A (en) * 2021-11-10 2022-03-04 上海建工四建集团有限公司 Use method of full-automatic control type vacuum deep well device
CN114134918B (en) * 2021-11-10 2023-08-08 上海建工四建集团有限公司 Use method of full-automatic control type vacuum deep well device

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