JPH0573455B2 - - Google Patents

Info

Publication number
JPH0573455B2
JPH0573455B2 JP19738390A JP19738390A JPH0573455B2 JP H0573455 B2 JPH0573455 B2 JP H0573455B2 JP 19738390 A JP19738390 A JP 19738390A JP 19738390 A JP19738390 A JP 19738390A JP H0573455 B2 JPH0573455 B2 JP H0573455B2
Authority
JP
Japan
Prior art keywords
liquid
container
liquid level
pipe
water
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 - Lifetime
Application number
JP19738390A
Other languages
Japanese (ja)
Other versions
JPH0483527A (en
Inventor
Kensuke Akamatsu
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.)
Espec Corp
Original Assignee
Tabai Espec Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Tabai Espec Co Ltd filed Critical Tabai Espec Co Ltd
Priority to JP19738390A priority Critical patent/JPH0483527A/en
Publication of JPH0483527A publication Critical patent/JPH0483527A/en
Publication of JPH0573455B2 publication Critical patent/JPH0573455B2/ja
Granted legal-status Critical Current

Links

Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J4/00Feed or outlet devices; Feed or outlet control devices
    • B01J4/02Feed or outlet devices; Feed or outlet control devices for feeding measured, i.e. prescribed quantities of reagents

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Feeding, Discharge, Calcimining, Fusing, And Gas-Generation Devices (AREA)

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は閉じられた容器へ所定液量に給液する
方法に関する。
DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a method for dispensing a predetermined amount of liquid into a closed container.

〔従来の技術〕[Conventional technology]

閉じられた容器へ所定液量に給液しなければな
らない場合は種々考えられるが、その一例を挙げ
ると、各種材料、各種機器の部品、各種機器、装
置類等の温度および温度下における影響を調べる
ための恒温恒湿器において使用される湿度制御の
ための飽和空気発生槽を挙げることができる。
There are various cases in which a predetermined amount of liquid must be supplied to a closed container, but one example is the temperature of various materials, parts of various equipment, various equipment, devices, etc., and the influence of the temperature. An example is a saturated air generation tank for humidity control used in a constant temperature and humidity chamber for testing.

従来、このような飽和空気発生槽の如き閉じら
れた容器へ所定水位あるいは所定水量に給水を行
う場合は、一般に、容器内の所定水位とほぼ同レ
ベルに配置した水位調節器を該容器に連通させ、
該調節器におけるフロートスイツチのような液位
検知手段によつて、容器内水位を検出しながら所
定推量を得るように給水し、容器に圧力がかかる
場合は容器と水位調節器の気相部を均圧管でつな
ぐという方式が採用されており、この他、容器に
直接液位レベル計を取り付ける方法が採用される
こともあつた。
Conventionally, when supplying water to a predetermined water level or amount to a closed container such as a saturated air generating tank, a water level regulator placed at approximately the same level as the predetermined water level in the container is generally connected to the container. let me,
A liquid level detection means such as a float switch in the regulator supplies water to obtain a predetermined amount of water while detecting the water level in the container, and when pressure is applied to the container, the gas phase part of the container and water level regulator is A method of connecting with pressure equalizing pipes was adopted, and in some cases, a method of attaching a liquid level gauge directly to the container was also adopted.

〔発明が解決しようとする課題〕[Problem to be solved by the invention]

しかし、前記液位調節器を採用する場合には、
その取り付け位置に制限があり、また、容器に圧
力がかかる場合には前述のとおり均圧管を必要と
するので、該均圧管の取り付けが面倒であるう
え、それが嵩張るという問題もあつた。
However, when adopting the liquid level regulator,
There are restrictions on the mounting position, and when pressure is applied to the container, a pressure equalizing tube is required as described above, so there are problems in that the pressure equalizing tube is troublesome to attach and is bulky.

容器に直接液位レベル計を取り付ける方式で
は、例えば、該容器が前記飽和空気発生槽のよう
に該容器内の液体の温度制御するためのブライン
に埋沈されるような場合には、該レベル計の取り
付け構造が複雑になるほか、様々な取り付け上の
制約があり、飽和空気発生装置の構造によつては
取り付けが不可能な場合もあつた。
In the method of attaching a liquid level gauge directly to a container, for example, when the container is submerged in brine for controlling the temperature of the liquid in the container, such as in the saturated air generation tank, the level In addition to complicating the installation structure of the meter, there were various installation restrictions, and installation was sometimes impossible depending on the structure of the saturated air generator.

そこで本発明は、閉じられた容器への給液方法
であつて、液位調節器により該容器内液量を所定
のものに調節することができ、しかも、該液位調
節器を容器内に所定液位にはほぼ一致するように
配置しなければならないという制限がなく、均圧
管も必要としない給液方法を提供することを目的
とする。
Therefore, the present invention provides a method for supplying liquid to a closed container, in which the amount of liquid in the container can be adjusted to a predetermined level using a liquid level regulator, and the liquid level regulator is installed inside the container. It is an object of the present invention to provide a liquid supply method that does not require a pressure equalizing pipe and is not limited to the arrangement that the liquid level must be substantially coincident with a predetermined liquid level.

〔課題を解決するための手段〕[Means to solve the problem]

前記目的を達成する本発明方法は、閉じられた
容器へ給液方法であつて、前記容器の上部気相部
に液供給管を接続するとともに該容器の下部液相
部に所定液位に開口する溢液管を接続し、液流入
口および排液口を有するとともに液位検知手段を
備え、前記液流入口面積が前記排液口面積より大
きい液位調節器の該液流入口を前記溢液管に接続
し、前記液供給管から前記容器へ給液し、前記所
定液位を超える液を前記溢液管から前記液位調節
器へ流入させ、且つ、前記液位調節器における液
流入量が排出量より多くなるように前記給液を行
い、該液位調節器内液位の上昇により前記液位検
知手段が作動すると前記給液を停止するとともに
前記溢液管を閉じることを特徴とする。
The method of the present invention for achieving the above object is a method for supplying liquid to a closed container, which includes connecting a liquid supply pipe to an upper gas phase portion of the container and opening an opening at a predetermined liquid level to a lower liquid phase portion of the container. A liquid overflow pipe is connected to the liquid level regulator, which has a liquid inlet and a liquid drain, and is provided with a liquid level detection means, and the liquid inlet has a larger area than the liquid drain. connecting to a liquid pipe, supplying liquid from the liquid supply pipe to the container, causing liquid exceeding the predetermined liquid level to flow from the overflow pipe to the liquid level regulator, and causing liquid to flow into the liquid level regulator. The liquid is supplied so that the amount is greater than the discharge amount, and when the liquid level detecting means is activated due to a rise in the liquid level in the liquid level regulator, the liquid supply is stopped and the overflow pipe is closed. shall be.

前記方法において、給液を予め定めた時間間隔
で行えば、前記容器水量を常時ほぼ一定に維持す
ることができる。
In the method, if the liquid is supplied at predetermined time intervals, the amount of water in the container can be maintained substantially constant at all times.

前記容器は単一の容器のほか、種々のタイプも
のが考えられ、例えば、前記容器が、上下に複数
段に配置された小容器からなる場合、各上下に隣
合う小容器は、上端が上段小容器の所定液位に開
口し、下端が下段小容器の気相部に開口する管に
より接続し、前記液供給管を最上段小容器の気相
部に接続し、前記溢水管上端を最下段小容器の所
定液位に開口させる。
In addition to a single container, the container may be of various types. For example, if the container is composed of small containers arranged in multiple tiers above and below, each of the vertically adjacent small containers has an upper end that is connected to the upper tier. The liquid supply pipe is connected to the gas phase part of the uppermost small container, and the upper end of the overflow pipe is connected to the gas phase part of the uppermost small container. Open the lower small container to the specified liquid level.

〔作用〕[Effect]

本発明給液方法によると、液は液供給管から容
器内へ供給され、それによつて容器内液量が増加
し、液が溢液管の開口位置まで達すると、それを
超える液は該溢液管から流出して液位調節器内へ
流入する。該調節器の液流入口面積は排液口面積
より大きくされているので、液位調節器への液流
入量は該調節器からの排液量よりも多く、従つて
液位調節器内には次第に液が溜まり液位が上昇す
る。該液位上昇により液位検知手段が作動する
と、容器内への液供給が停止され、溢液管が閉じ
られる。その後、液位調節器内の液は落下放出さ
れ、次の液位調節に備えられる。
According to the liquid supply method of the present invention, the liquid is supplied from the liquid supply pipe into the container, thereby increasing the amount of liquid in the container, and when the liquid reaches the opening position of the overflow pipe, the liquid beyond that point is removed from the overflow. It flows out from the liquid pipe and flows into the liquid level regulator. Since the liquid inlet area of the regulator is larger than the liquid outlet area, the amount of liquid flowing into the liquid level regulator is greater than the amount of liquid draining from the regulator, and therefore, the amount of liquid flowing into the liquid level regulator is greater than the amount of liquid flowing out from the regulator. The liquid gradually accumulates and the liquid level rises. When the liquid level detection means is activated due to the rise in the liquid level, the supply of liquid into the container is stopped and the overflow pipe is closed. Thereafter, the liquid in the liquid level regulator is discharged and is ready for the next liquid level adjustment.

容器への給液を予め定めた時間間隔で行えば、
前記動作が繰り返され、容器内液量は常時ほぼ一
定に維持される。
If the liquid is supplied to the container at predetermined time intervals,
The above operation is repeated, and the amount of liquid in the container is kept almost constant at all times.

〔実施例〕〔Example〕

以下本発明の一実施例を図面を参照して説明す
る。
An embodiment of the present invention will be described below with reference to the drawings.

以下に説明する実施例は、恒温恒湿器の飽和空
気発生装置における飽和空気発生槽に所定水量に
給水を行う場合である。
The embodiment described below is a case where a predetermined amount of water is supplied to a saturated air generation tank in a saturated air generation device of a constant temperature and humidity chamber.

第1図は恒温恒温器の概略構成を示しており、 この恒温恒湿器Aは、試験槽1をブライン槽2
のブライン20中に埋沈させ、該ブラインを図示
しない温度制御手段により所定温度に制御するこ
とにより試験槽1内温度とし、試験槽1へは飽和
空気発生装置3から飽和空気を導入するように
し、飽和空気の導入に伴つて試験槽の気体の一部
を図示しない排気孔から外部へ排出するように構
成したものである。
Figure 1 shows the schematic configuration of a constant temperature and humidity chamber. This temperature and humidity chamber A consists of a test chamber 1 and a brine chamber 2.
The internal temperature of the test tank 1 is set by submerging the brine in a brine 20 and controlling the brine to a predetermined temperature by a temperature control means (not shown), and saturated air is introduced into the test tank 1 from a saturated air generator 3. The test chamber is configured such that as saturated air is introduced, a portion of the gas in the test chamber is discharged to the outside through an exhaust hole (not shown).

飽和空気発生装置3は、第2図にその詳細を示
すように、ブラインBを収容したブライン槽31
を備え、ブラインBは槽内部に配置したブライン
温度制御用のヒータ32および冷却器33の一方
または双方の使用で所定温度に制御される。
As shown in detail in FIG. 2, the saturated air generator 3 includes a brine tank 31 containing brine B.
The brine B is controlled to a predetermined temperature by using one or both of a heater 32 and a cooler 33 for brine temperature control arranged inside the tank.

ブラインB中には飽和空気発生槽34が埋沈さ
れており、図示しない支持手段によりブライン槽
31に支持されている。飽和空気発生槽34は密
閉された上段槽341と下段槽342とからなつ
ており、上段槽341の液槽部341bには所定
水位に上端が開口した接続管343が設けられ、
該管の下端は下段槽342の気相部342aに開
口している。
A saturated air generation tank 34 is buried in the brine B, and is supported by the brine tank 31 by support means (not shown). The saturated air generation tank 34 consists of a sealed upper tank 341 and a lower tank 342, and a liquid tank portion 341b of the upper tank 341 is provided with a connecting pipe 343 whose upper end is open at a predetermined water level.
The lower end of the tube opens into the gas phase section 342a of the lower tank 342.

上段槽341の気相部341aは電磁弁41を
途中に有する管42によつて前記試験室1に接続
されており、下段槽342の気相部342aは途
中に電磁弁51を有する管52によつて乾燥空気
発生槽53に接続されている。
The gas phase part 341a of the upper tank 341 is connected to the test chamber 1 by a pipe 42 having a solenoid valve 41 in the middle, and the gas phase part 342a of the lower tank 342 is connected to a pipe 52 having a solenoid valve 51 in the middle. Therefore, it is connected to a dry air generation tank 53.

上段および下段の各槽には水Wが入れられてお
り、その水温はブラインBによつて所定温度に制
御される。水Wは、得ようとする飽和空気によつ
ては凍結される場合もある。この状態で電磁弁5
1を開くことにより乾燥空気発生槽53から下段
槽342に供給された乾燥空気は下段槽342に
おいて水面に接触しつつ管343を通つて上段槽
341に入り、ここでも水面と接触し飽和空気と
なつて電磁弁41および管42を通つて試験槽1
へ供給される。なお、水Wを凍結させて用いる場
合は、前記水面は凍結水面である。
Water W is placed in each of the upper and lower tanks, and the water temperature is controlled by brine B to a predetermined temperature. The water W may be frozen depending on the saturated air to be obtained. In this state, solenoid valve 5
1 is opened, the dry air supplied from the dry air generation tank 53 to the lower tank 342 enters the upper tank 341 through the pipe 343 while contacting the water surface in the lower tank 342, where it also comes into contact with the water surface and becomes saturated air. The test chamber 1 is passed through the solenoid valve 41 and the pipe 42.
supplied to Note that when the water W is frozen and used, the water surface is a frozen water surface.

試験槽1に供給される飽和空気は途中でブライ
ン20により加熱されるとともに該試験槽におい
ても加熱され、所定温度および湿度の空気とな
る。また、この飽和空気供給に伴つて試験槽1内
の気体の一部は図示しない排気孔から外部へ押し
出される。
The saturated air supplied to the test tank 1 is heated by the brine 20 along the way and is also heated in the test tank, so that the air has a predetermined temperature and humidity. Further, as the saturated air is supplied, a part of the gas in the test chamber 1 is pushed out from an exhaust hole (not shown).

飽和空気発生槽34への水の供給は、本発明方
法に従つて次のように行われる。
Water is supplied to the saturated air generation tank 34 according to the method of the present invention as follows.

すなわち、上段槽341の気相部341aに水
供給管61を接続し、該管61は電磁弁62およ
びポンプ63を介して常温下の水タンク64に接
続する。一方、下段糟342の液糟部342bに
は該糟内の所定水位に開口する溢水管71を設け
るとともに該管をブライン糟31の底壁を貫通さ
せてプライン糟下方へ延ばし、水位調節器8の水
流入口81に接続する。水位調節器8の排水孔8
2には排水管9を接続しておく。溢水管71の途
中には電磁弁72を設けておく。
That is, a water supply pipe 61 is connected to the gas phase portion 341a of the upper tank 341, and the pipe 61 is connected to a water tank 64 at normal temperature via a solenoid valve 62 and a pump 63. On the other hand, an overflow pipe 71 that opens to a predetermined water level in the brine tank is provided in the liquid tank part 342b of the lower stage brine tank 342, and the pipe is passed through the bottom wall of the brine tank 31 and extended downward into the brine tank, and a water level regulator 8 It is connected to the water inlet 81 of. Drain hole 8 of water level regulator 8
A drain pipe 9 is connected to 2. A solenoid valve 72 is provided in the middle of the overflow pipe 71.

ここで、水位調節器8の水流入口81の開口面
積は排水孔82の開口面積より大きくしておくと
ともに、溢水管71および前記接続管343の各
内径は排水管9の内径よりも大きくしておく。
Here, the opening area of the water inlet 81 of the water level regulator 8 is made larger than the opening area of the drain hole 82, and the inner diameters of the overflow pipe 71 and the connecting pipe 343 are made larger than the inner diameter of the drain pipe 9. put.

このような準備のもとに、電磁弁62を開くと
もにポンプ63を運転し、水タンク64から水を
上段糟341へ供給する。これによつて上段糟3
41内の水位は上昇し、該水位が管343の上端
開口に達すると、それから後に供給される水は該
管343を通つて下段糟342へ流入し始める。
下段糟342への水流入により該糟内の水位が上
昇し、水位が溢水管71の上端開口を超え始める
と、水は該溢水管71を通つて水位調節器8へ流
入し、さらに排水孔82、排水管9から外部へ排
出される。前記水供給管61による水の供給量
は、溢水管71を介して水流入口81から水位調
節器8へ流入する水量が、該調節器の排水口82
から外部へ排出される水量より大きくなるように
設定しておく。
Under these preparations, the solenoid valve 62 is opened and the pump 63 is operated to supply water from the water tank 64 to the upper tank 341. With this, the upper stage 3
The water level in 41 rises and when it reaches the upper opening of tube 343, the water that is subsequently supplied begins to flow through the tube 343 into the lower chamber 342.
When the water inflow into the lower cassette 342 causes the water level in the cassette to rise and the water level begins to exceed the upper end opening of the overflow pipe 71, the water flows into the water level regulator 8 through the overflow pipe 71, and then flows through the drain hole. 82, is discharged to the outside from the drain pipe 9. The amount of water supplied by the water supply pipe 61 is such that the amount of water flowing into the water level regulator 8 from the water inlet 81 via the overflow pipe 71 is equal to the amount of water flowing into the water level regulator 8 from the drain port 82 of the regulator.
Set it so that it is larger than the amount of water discharged to the outside.

かくして、水位調節器8内の水位は、水流入量
と排出量の差により次第に上昇し、それによつて
該調節器における水位検知手段(本例ではフロー
トスイツチ)83が作動し、上段糟341および
下段糟342において、水位が所定水位にあるこ
とを知らせる信号を制御部10に送る。制御部は
この信号によつて給水側のポンプ63を停止させ
るとともに電磁弁62を閉じ、同時に溢水管71
における電磁弁72を閉じる。かくして、飽和空
気発生槽34の各槽に所定水量に水が溜められ
る。その後は水位調節器8内の液を落下放出さ
せ、次の水位調節に備える。
In this way, the water level in the water level regulator 8 gradually rises due to the difference between the inflow and discharge amounts of water, and the water level detecting means (in this example, a float switch) 83 in the regulator is activated, and the upper chamber 341 and In the lower tank 342, a signal is sent to the control unit 10 to inform that the water level is at a predetermined water level. Based on this signal, the control unit stops the pump 63 on the water supply side, closes the solenoid valve 62, and at the same time closes the overflow pipe 71.
Close the solenoid valve 72 at. In this way, each tank of the saturated air generation tank 34 is filled with a predetermined amount of water. Thereafter, the liquid in the water level regulator 8 is allowed to fall and discharge, in preparation for the next water level adjustment.

制御部10には、予め定めた一定時間間隔でポ
ンプ63を運転し、且つ、電磁弁62および71
を開くようにさせ、それによつて上段および下段
の各槽に常時ほぼ一定量の水が存在するように制
御させる。
The control unit 10 operates the pump 63 at predetermined fixed time intervals, and has electromagnetic valves 62 and 71.
It is controlled so that a substantially constant amount of water is always present in each of the upper and lower tanks.

以上説明した実施例方法によると、水位調節器
を用いて飽和空気発生槽34内の水位ないし水量
を所定のものに制御するにもかかわらず、水位調
節器は飽和空気発生槽内の所定水位とほぼ同レベ
ルに配置する必要がなく、そのようなレベルへの
水位調節器の配置が困難な場合に極めて便利であ
るとともに、水位調節器と飽和空気発生槽34と
を均圧管で接続する必要もない。
According to the embodiment method described above, although the water level regulator is used to control the water level or water amount in the saturated air generation tank 34 to a predetermined level, the water level regulator does not control the water level or the amount of water in the saturated air generation tank 34 to a predetermined level. It is not necessary to arrange the water level regulator at almost the same level, and it is extremely convenient when it is difficult to arrange the water level regulator at such a level, and there is no need to connect the water level regulator and the saturated air generation tank 34 with a pressure equalizing pipe. do not have.

なお、本発明は前記実施例に限定されるもので
はなく、他には種々の態様で実施することができ
る。例えば、飽和空気発生槽34は前記例では上
下と小容器からなつているが、さらに多くと容器
からなつていてもよく、逆に、単一の容器からな
つていてもよい。いずれの場合にも本発明を適用
できる。また、本発明は前記実施例の飽和空気発
生槽だけでなく、広く一般に、閉じられた容器へ
液(水に限定されない)を供給する場合に適用で
きる。
It should be noted that the present invention is not limited to the above embodiments, and can be implemented in various other ways. For example, although the saturated air generation tank 34 is made up of upper and lower containers and a small container in the above example, it may be made up of more containers, or conversely, it may be made up of a single container. The present invention can be applied to any case. Further, the present invention can be applied not only to the saturated air generation tank of the above embodiment, but also to a wide range of applications in which liquid (not limited to water) is supplied to a closed container.

〔発明の効果〕〔Effect of the invention〕

以上説明したように本発明によると、閉じられ
た容器への給液方法であつて、液位調節器により
該容器内液量を所定のものに調節することがで
き、しかも、該液位調節器を容器内の所定液位に
ほぼ一致するように配置しなければならないとい
う制限がなく、均圧管も必要としない給液方法を
提供することができる。
As explained above, according to the present invention, there is provided a method for supplying liquid to a closed container, in which the amount of liquid in the container can be adjusted to a predetermined value using a liquid level regulator, and the liquid level can be adjusted to a predetermined value. It is possible to provide a liquid supply method without the restriction that the container must be arranged so as to approximately correspond to a predetermined liquid level in the container, and without the need for a pressure equalizing pipe.

容器への給液を予め定めた時間間隔で行うとき
は、容器内液量は常時ほぼ一定に維持される。
When liquid is supplied to the container at predetermined time intervals, the amount of liquid in the container is always maintained substantially constant.

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

第1図は本発明方法を適用する恒温恒湿器の概
略構成図、第2図は飽和空気発生装置の要部断面
図である。 A……恒温恒湿器、1……試験槽、2……ブラ
イン槽、20……ブライン、3……飽和空気発生
装置、31……ブライン槽、34……飽和空気発
生槽、341……上段槽、342……下段槽、3
41a,342a……気相部、341b,342
b……液相部、343……接続管、61……水供
給管、62……電磁弁、63……ポンプ、64…
…水タンク、71……溢水管、72……電磁弁、
8……水位調節器、81……水流入口、82……
排水口、83……フロートスイツチ、9……排水
管、10……制御部。
FIG. 1 is a schematic configuration diagram of a constant temperature and humidity chamber to which the method of the present invention is applied, and FIG. 2 is a sectional view of essential parts of a saturated air generator. A... Constant temperature and humidity chamber, 1... Test tank, 2... Brine tank, 20... Brine, 3... Saturated air generator, 31... Brine tank, 34... Saturated air generation tank, 341... Upper tank, 342...Lower tank, 3
41a, 342a...gas phase part, 341b, 342
b...liquid phase section, 343...connecting pipe, 61...water supply pipe, 62...electromagnetic valve, 63...pump, 64...
...Water tank, 71...Overflow pipe, 72...Solenoid valve,
8...Water level regulator, 81...Water inlet, 82...
Drain port, 83...Float switch, 9...Drain pipe, 10...Control unit.

Claims (1)

【特許請求の範囲】 1 閉じられた容器への給液方法であつて、前記
容器の上部気相部に液供給管を接続するとともに
該容器の下部液相部に所定液位に開口する溢液管
を接続し、液流入口および排液口を有するととも
に液位検知手段を備え、前記液流入口面積が前記
排液口面積より大きい液位調節器の該液流入口を
前記溢液管に接続し、前記液供給管から前記容器
へ給液し、前記所定液位を超える液を前記溢液管
から前記液位調節器へ流入させ、且つ、前記液位
調節器における液流入量が排出量より多くなるよ
うに前記給液を行い、該液位調節器内液位の上昇
により前記液位検知手段が作動すると前記給液を
停止するとともに前記溢液管を閉じることを特徴
とする給液方法。 2 前記給液を予め定めた時間間隔で行うことに
より前記容器内液量を常時略一定に維持する請求
項1記載の給液方法。 3 前記容器が、上下に複数段に配置された小容
器からなり、各上下に隣合う小容器は、上端が上
段小容器の所定液位に開口し、下端が下段小容器
の気相部に開口する管により接続されており、前
記液供給管を最上段小容器の気相部に接続し、前
記溢水管上端を最下段小容器の所定液位に開口さ
せた請求項1または2記載の給液方法。
[Scope of Claims] 1. A method for supplying liquid to a closed container, which includes connecting a liquid supply pipe to an upper gas phase portion of the container and providing an overflow opening to a predetermined liquid level in a lower liquid phase portion of the container. A liquid level regulator is connected to a liquid pipe, and has a liquid inlet and a liquid drain, and is provided with liquid level detection means, and the liquid inlet has a larger area than the liquid drain, and the liquid inlet is connected to the overflow pipe. , the liquid is supplied from the liquid supply pipe to the container, and the liquid exceeding the predetermined liquid level flows into the liquid level regulator from the overflow pipe, and the amount of liquid flowing into the liquid level regulator is The liquid is supplied so as to be larger than the discharge amount, and when the liquid level detecting means is activated due to a rise in the liquid level in the liquid level regulator, the liquid supply is stopped and the overflow pipe is closed. Liquid supply method. 2. The liquid supply method according to claim 1, wherein the liquid amount in the container is always maintained substantially constant by performing the liquid supply at predetermined time intervals. 3. The container is composed of small containers arranged in a plurality of vertically arranged tiers, and the upper end of each vertically adjacent small container opens to a predetermined liquid level in the upper tier small container, and the lower end opens to the gas phase part of the lower tier tier small container. 3. The liquid supply pipe is connected to a gas phase portion of the uppermost small container, and the upper end of the overflow pipe is opened to a predetermined liquid level of the lowermost small container. Liquid supply method.
JP19738390A 1990-07-25 1990-07-25 Method for supplying liquid to closed container Granted JPH0483527A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP19738390A JPH0483527A (en) 1990-07-25 1990-07-25 Method for supplying liquid to closed container

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP19738390A JPH0483527A (en) 1990-07-25 1990-07-25 Method for supplying liquid to closed container

Publications (2)

Publication Number Publication Date
JPH0483527A JPH0483527A (en) 1992-03-17
JPH0573455B2 true JPH0573455B2 (en) 1993-10-14

Family

ID=16373602

Family Applications (1)

Application Number Title Priority Date Filing Date
JP19738390A Granted JPH0483527A (en) 1990-07-25 1990-07-25 Method for supplying liquid to closed container

Country Status (1)

Country Link
JP (1) JPH0483527A (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102013216457A1 (en) 2013-08-20 2015-02-26 Efficient Energy Gmbh THERMODYNAMIC DEVICE AND METHOD FOR MANUFACTURING A THERMODYNAMIC DEVICE

Also Published As

Publication number Publication date
JPH0483527A (en) 1992-03-17

Similar Documents

Publication Publication Date Title
US4607658A (en) Water level control device
US5815637A (en) Humidifier for control of semi-conductor manufacturing environments
US5254292A (en) Device for regulating and reducing the fluctuations in a polyphasic flow, and its use
CN100501230C (en) Steam generation method and apparatus for simulation laboratory
JP2003214989A (en) Engine oil level control system
JPS617908A (en) Liquid surface controller
KR101962402B1 (en) Pipe structure and installation method for water quality measuring instrument
JPH0483527A (en) Method for supplying liquid to closed container
US4671099A (en) Device for measuring the thermodynamic characteristics of a fluid
RU2299321C2 (en) Method and device for oil and gas-condensate well production measurement in air-tight oil collection systems
CN107991462A (en) A kind of simulation test device and its test method for water and soil conservation
JPH03105217A (en) Differential pressure type water level measuring device
JPS6158718B2 (en)
KR100742367B1 (en) Chemical Mixing Feeder
JP4096129B2 (en) Droplet dropping device
JPH0857224A (en) Circulation system for liquid to be treated
JPH0236118Y2 (en)
JPS5854705Y2 (en) gas detector
JPH0446814Y2 (en)
JPH0686975B2 (en) Adsorption amount measuring device
SU1376736A1 (en) Device for sampling fluid for trunk pipeline
JPH082559Y2 (en) Free float type drain trap
JPS6219217B2 (en)
SU1161775A1 (en) Cryogenic pipeline
SU1432469A1 (en) Pressure regulator for water-supply systems

Legal Events

Date Code Title Description
R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

FPAY Renewal fee payment (prs date is renewal date of database)

Free format text: PAYMENT UNTIL: 20071014

Year of fee payment: 14

FPAY Renewal fee payment (prs date is renewal date of database)

Year of fee payment: 15

Free format text: PAYMENT UNTIL: 20081014

FPAY Renewal fee payment (prs date is renewal date of database)

Free format text: PAYMENT UNTIL: 20091014

Year of fee payment: 16

FPAY Renewal fee payment (prs date is renewal date of database)

Year of fee payment: 17

Free format text: PAYMENT UNTIL: 20101014

EXPY Cancellation because of completion of term
FPAY Renewal fee payment (prs date is renewal date of database)

Year of fee payment: 17

Free format text: PAYMENT UNTIL: 20101014