JPS63130107A - Automatic deaerator - Google Patents

Automatic deaerator

Info

Publication number
JPS63130107A
JPS63130107A JP27389186A JP27389186A JPS63130107A JP S63130107 A JPS63130107 A JP S63130107A JP 27389186 A JP27389186 A JP 27389186A JP 27389186 A JP27389186 A JP 27389186A JP S63130107 A JPS63130107 A JP S63130107A
Authority
JP
Japan
Prior art keywords
deaeration
liquid
bottle
degassing
valve
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
JP27389186A
Other languages
Japanese (ja)
Inventor
Toshiaki Imai
敏明 今井
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
Original Assignee
Toshiba 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 filed Critical Toshiba Corp
Priority to JP27389186A priority Critical patent/JPS63130107A/en
Publication of JPS63130107A publication Critical patent/JPS63130107A/en
Pending legal-status Critical Current

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  • Degasification And Air Bubble Elimination (AREA)
  • Physical Water Treatments (AREA)

Abstract

PURPOSE:To enhance deaeration velocity and to miniaturize the title apparatus by providing a vibrator for vibrating liquid in the case of deaerating liquid by evacuating it. CONSTITUTION:Air is drawn from a deaeration bottle 5 by closing an on-off valve 12 on an outlet side and opening an on-off valve 4 on an inlet side and actuating an exhaust pump 9, and the inside of the bottle 5 is evacuated and raw liquid 1 is introduced therein and when the raw liquid 1 is sufficiently introduced by means of a liquid level sensor 11, the valve 4 is closed and the inside of the bottle 5 is made to a state of negative pressure and gas incorporated in the raw liquid 1 is deaerated. In this case, the raw liquid 1 is agitated by rotation of a rotator 10 such as a magnetic stirrer or by ultrasonic wave or the like and vibration is given and deaeration velocity is enhanced. In such a way, the apparatus can be miniaturized since deaeration is efficiently performed.

Description

【発明の詳細な説明】 [発明の目的] (産業上の利用分野) 本発明は液体を引用にして脱気する自動脱気装置に関す
る。
DETAILED DESCRIPTION OF THE INVENTION [Object of the Invention] (Industrial Application Field) The present invention relates to an automatic degassing device for degassing a liquid.

例えば自動化学分析装置に於る反応セルを一定温度(例
えば37°C)に恒温するために恒温槽に供給される恒
温水を脱気するのに用いたり、成るいは試薬ポンプやサ
ンプルポンプ等て使用される純水な脱気するのに用いら
れる自動脱気装置に関するものである。
For example, it can be used to degas constant temperature water supplied to a constant temperature bath to keep a reaction cell at a constant temperature (e.g. 37°C) in an automatic chemical analyzer, or it can be used for reagent pumps, sample pumps, etc. This invention relates to an automatic degassing device used for degassing pure water.

(従来の技術) 第2図及び第3図にこの種脱気装置の従来例を示す。(Conventional technology) FIGS. 2 and 3 show conventional examples of this type of deaerator.

先ず第2図に示す従来例について説明する。First, the conventional example shown in FIG. 2 will be explained.

第2図に於てlは脱気すべき原液てあり、原液容器2に
入っている。この原液1は、排気ポンプ9により脱気瓶
5内を負圧にしたとき、入口側チューブ3を通って鋭気
瓶5内に流入する。4は入口側開閉弁であり、入口側チ
ューブ3の流路を開閉する。
In FIG. 2, l represents the stock solution to be degassed, which is contained in the stock solution container 2. When the inside of the deaeration bottle 5 is made to have a negative pressure by the exhaust pump 9, this stock solution 1 flows into the deaeration bottle 5 through the inlet tube 3. Reference numeral 4 denotes an inlet side opening/closing valve, which opens and closes the flow path of the inlet side tube 3.

脱気瓶5は耐圧容器であって、原液lを貯溜し、減圧を
保持する機能を有する。また、その底部にヒータ20を
備えている。
The deaeration bottle 5 is a pressure-resistant container, and has the function of storing the stock solution 1 and maintaining a reduced pressure. Furthermore, a heater 20 is provided at the bottom.

6は脱気瓶蓋であり、脱気瓶5を密閉するとともに、排
気チューブ7を貫通保持している。
A deaeration bottle lid 6 seals the deaeration bottle 5 and holds the exhaust tube 7 therethrough.

排気ポンプ9は脱気類5内を低圧にするためのポンプで
あり、排気チューブ7を通して脱気類5に連結している
The exhaust pump 9 is a pump for making the inside of the degassing unit 5 low pressure, and is connected to the degassing unit 5 through an exhaust tube 7.

11は液面センサであり、脱気類5中の水位を測定する
機能を有する。
11 is a liquid level sensor, which has a function of measuring the water level in the deaerator 5.

12は出口側開閉弁であり、出口側チューブ14の流路
の開閉を行う機能を有する。
Reference numeral 12 denotes an outlet side opening/closing valve, which has a function of opening and closing the flow path of the outlet side tube 14.

15は脱気水容器てあり、脱気類5て作られた脱気水1
6を一時溜める容器である。
15 is a deaerated water container, which contains deaerated water 1 made from deaerated water 5
This is a container that temporarily stores 6.

17は脱気水16を図示しない他のポンプなどに導くチ
ューブであり、このチューブ17を通じて脱気水16か
図示しない自動化学分析装置の恒温槽やポンプ等に供給
される。
Reference numeral 17 denotes a tube that leads the degassed water 16 to another pump (not shown), and through this tube 17, the degassed water 16 is supplied to a constant temperature bath, pump, etc. of an automatic chemical analyzer (not shown).

18は前記脱気瓶蓋6に設けた圧力センサであり、脱気
類5内の圧力を検出して制御装置に信号を送り、制御装
置によって排気ポンプ9の制御を行う。
Reference numeral 18 denotes a pressure sensor provided on the deaeration bottle lid 6, which detects the pressure inside the deaeration unit 5 and sends a signal to the control device, which controls the exhaust pump 9.

19は液面センサであり、脱気水容器15中の水位を測
定する機能を有する。
A liquid level sensor 19 has a function of measuring the water level in the deaerated water container 15.

以上のような従来の脱気装置は、出口側開閉弁12を閉
じ、入口側開閉弁4を開けて排気ポンプ9を動作させる
と、空気は脱気類5より抜け、脱気類5中か減圧になり
、FX液lか入口側チューブ3を通って脱気類5内に入
る。
In the conventional degassing device as described above, when the outlet side on-off valve 12 is closed, the inlet side on-off valve 4 is opened and the exhaust pump 9 is operated, air escapes from the deaeration unit 5 and air is removed from the deaeration unit 5. The pressure is reduced, and the FX liquid 1 passes through the inlet tube 3 and enters the deaerator 5.

脱気類5中に原液lが充分に入り、液面センサ11が充
分に原液1が入ワたことを検出すると。
When the stock solution 1 has sufficiently entered the deaerator 5 and the liquid level sensor 11 detects that the stock solution 1 has sufficiently entered.

図示しない制御装置か入口側開閉弁4を閉しる。A control device (not shown) closes the inlet side on-off valve 4.

その後排気ポンプ9が排気動作を続けると脱気類5の中
は所定の負圧状態となり、原液中の気体が脱気される。
Thereafter, when the exhaust pump 9 continues the exhaust operation, the interior of the deaerator 5 becomes a predetermined negative pressure state, and the gas in the stock solution is degassed.

そしてこの際、ヒータ20て原液1を加熱することによ
って脱気作用を高めている。
At this time, the deaeration effect is enhanced by heating the stock solution 1 using the heater 20.

この間圧力センサ18は、脱気類5内の圧力を検出し、
制御装置に信号を送り、制御装置による排気ポンプ9の
制御を行なう、そして予め決められた一定時間が経過す
ると、排気ポンプ9か動作を停止し、出口側開閉弁12
が開いて脱気類5中の脱気された液体が出口側チューブ
14を通って脱気水容器15へ流れる。
During this time, the pressure sensor 18 detects the pressure inside the deaerator 5,
A signal is sent to the control device, and the control device controls the exhaust pump 9. When a predetermined period of time has elapsed, the operation of the exhaust pump 9 is stopped, and the outlet side on-off valve 12 is stopped.
is opened and the degassed liquid in the deaerator 5 flows through the outlet tube 14 to the degassed water container 15.

このようにして作られた脱気水16はチューブ17を通
って、恒温槽に供給されたり、成るいは試薬ポンプやサ
ンプルポンプ等で使用される。
The degassed water 16 thus produced is supplied to a constant temperature bath through a tube 17, or used in a reagent pump, sample pump, etc.

そして脱気水容器の液面センサ19か、脱気水容器15
内の脱気水16の液面を検知し脱気水16の残量か少な
いことを検知すると、再び上記脱気動作か繰返される。
Then, the liquid level sensor 19 of the degassed water container or the degassed water container 15
When the liquid level of the degassed water 16 inside is detected and it is detected that the remaining amount of the degassed water 16 is small, the above deaeration operation is repeated again.

次ぎに第3図に示す従来例について説明する。Next, a conventional example shown in FIG. 3 will be explained.

この脱気装置は、脱気法として膜分離法を用いており、
原水lか特殊合成樹脂膜21を通過するようになってい
る。この合成樹脂15i21は、圧力センサー22と制
御装置23と排気ポンプ24とで管理された真空容器2
5内に設置されており、水中に溶存している運動性の高
く分子サイズの小さな気体が115i壁を透過し分離排
出され送液ポンプ26によって装置出口から脱気水16
が供給されるようになっている。
This deaerator uses a membrane separation method as the deaeration method.
The raw water 1 passes through a special synthetic resin membrane 21. This synthetic resin 15i21 is stored in a vacuum container 2 controlled by a pressure sensor 22, a control device 23, and an exhaust pump 24.
The gas with high mobility and small molecular size dissolved in the water permeates through the 115i wall, is separated and discharged, and is sent to the degassed water 16 from the device outlet by the liquid feed pump 26.
is being supplied.

(発明が解決しようとする問題点) しかしながら以上のような従来の装置には。(Problem that the invention attempts to solve) However, the conventional devices such as those mentioned above.

次ぎのような問題点かある。There are some problems as follows.

先ず第2図に示した装置の場合、脱気類5の容量に比ベ
ヒータ20の容量か少ない場合液体の暖まる速度が小さ
く、脱気速度か遅くなるという欠点かある。
First, in the case of the apparatus shown in FIG. 2, if the capacity of the heater 20 is smaller than the capacity of the deaerator 5, the heating rate of the liquid is small and the degassing rate is slow.

次ぎに第3図に示した?を置の場合、例えば250℃で
約9ppmの溶存酸素を含んている水を1時間当り20
0.5pp−以下に脱気する場合、真空容器25内の引
圧な50 smoHにできるポンプを使用すると約ll
lの真空容器が必要であり装置が大型になるという欠点
がある。また、特殊合成樹脂膜21を大量に使用するた
め価格が高いという欠点もある。
Next, as shown in Figure 3? For example, at 250°C, water containing about 9 ppm of dissolved oxygen is heated at 20°C per hour.
When degassing to 0.5 pp- or less, if you use a pump that can create a suction pressure of 50 smoH in the vacuum container 25, the pressure will be approximately 11 liters.
This method has the disadvantage that it requires a vacuum container of 1 liter and the apparatus becomes large. Another disadvantage is that the price is high because a large amount of the special synthetic resin film 21 is used.

本発明の目的は、以上のような従来装置の問題点を解消
し、脱気速度が速く、小型でしかも低価格な自動脱気装
置を提供することにある。
SUMMARY OF THE INVENTION An object of the present invention is to solve the problems of the conventional devices as described above, and to provide an automatic degassing device that has a high degassing speed, is small in size, and is inexpensive.

[発明の構成] (問題点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、液体を引正にして脱
気する装置において、脱気中に液体を振動させる振動手
段を設けた構成とした。
[Structure of the Invention] (Means for Solving the Problems) In order to achieve the above object, the present invention provides an apparatus for deaerating a liquid by pulling the liquid, which is provided with a vibration means for vibrating the liquid during deaeration. The structure is as follows.

尚、ここで言う振動には攪拌も含んでいる。Note that the vibration referred to here also includes stirring.

(作用) 本発明は上記の構成としたのて、次のように作用する。(effect) With the above configuration, the present invention operates as follows.

即ち、真空脱気をする時、脱気される水を振動させると
脱気速度か速くなる。
That is, when performing vacuum deaeration, if the water to be deaerated is vibrated, the deaeration speed becomes faster.

そして本発明は先述した第2図の装置同様真空脱気方式
を採用しているので小型にでき、自動化学分析装置等に
内蔵することかできる。
Since the present invention employs a vacuum degassing method similar to the apparatus shown in FIG. 2 described above, it can be made compact and can be built into an automatic chemical analyzer or the like.

又、従来のように水を暖めて真空脱気を行なった場合に
は一旦上った水温を室温に戻す必要が生ずることもあっ
たか、本発明によれば水を暖める必要かないのて、上述
のような場合にいちいち水温を室温に戻す必要がない。
In addition, when water is warmed and vacuum degassed as in the past, it may be necessary to return the water temperature once it has risen to room temperature, but according to the present invention, there is no need to warm the water, so the above-mentioned method is possible. In such cases, there is no need to return the water temperature to room temperature each time.

更に本発明は第3図に示した装置とは異り、特殊合成樹
脂を用いてはいないのて価格も低価格で済む。
Furthermore, unlike the device shown in FIG. 3, the present invention does not use a special synthetic resin and is therefore inexpensive.

(実施例) 以下図示の実施例について説明する。(Example) The illustrated embodiment will be described below.

第1図は本発明に係る自動脱気装置の一実施例を示す概
略図であり、第2図に示した従来の装置と同様な部分に
ついては同一の符号を付しである0本実施例か従来の装
置と異る点は、従来のヒータ20に換え、振動手段とし
て脱気瓶5内に入れた回転体lOと、この回転体10の
駆動手段13とを設けた点にある。具体的には回転体1
0をマグネチックスターラで構成し、駆動手段13はこ
のマグネチックスターラを回転させる磁石を持つ回転体
を備えている。
FIG. 1 is a schematic diagram showing an embodiment of an automatic degassing device according to the present invention, and parts similar to those of the conventional device shown in FIG. 2 are denoted by the same reference numerals. The difference from the conventional apparatus is that, in place of the conventional heater 20, a rotating body 1O placed in a degassing bottle 5 and a driving means 13 for the rotating body 10 are provided as vibration means. Specifically, rotating body 1
0 is constituted by a magnetic stirrer, and the driving means 13 includes a rotating body having a magnet for rotating this magnetic stirrer.

以上のような脱気装置は、先述した従来の装置と略同様
な動作を行なうが、脱気の際、従来の装置が、ヒータ2
0て原液lを加熱することによって脱気作用を高めてい
たのに対し、本実施例では回転体lOを回すことにより
、液体11tWl拌してこれに振動を与え、脱気速度を
高めている点て異る。
The degassing device described above operates almost the same as the conventional device described above, but when degassing, the conventional device
Whereas the degassing effect was enhanced by heating the stock solution 1 at zero temperature, in this example, by rotating the rotating body 10, 11 tWl of liquid was stirred and vibrated, thereby increasing the degassing rate. Very different.

このような自動脱気装置に於て、lの脱気瓶を使って約
9ppmの溶存酸素を含んている水を5ppm以下にす
るのには、脱器瓶5内の圧力を50+uiHgにできる
ポンプを使用して、1時間当り、201の脱気水を製造
することかできた。尚、上記1時間には、脱器瓶5内の
圧力を50 mmHHにする時間と原液を脱器瓶5へ注
入し脱気された液を脱気水容器15へ移す時間とか含ま
れている。
In such an automatic degassing device, in order to reduce water containing approximately 9 ppm of dissolved oxygen to 5 ppm or less using a liter degassing bottle, a pump that can increase the pressure inside the degassing bottle 5 to 50 + uiHg is required. Using this, it was possible to produce 201 g of degassed water per hour. Incidentally, the above one hour includes the time to bring the pressure inside the degasser bottle 5 to 50 mmHH, the time to inject the stock solution into the degasser bottle 5, and the time to transfer the degassed liquid to the degassed water container 15. .

又、500slの瓶を使い、 4.51)Ill程度の
脱気水を製造した結果、3011/H程度製造すること
かできた。
In addition, using a 500 sl bottle, we were able to produce approximately 4.51) Ill of degassed water, resulting in approximately 3011/H.

以上本発明の一実施例について説明したか、本発明は上
記実施例に限定されるものではなく、本発明の要旨の範
囲内において適宜変形実施可能であることは言うまても
ない。
Although one embodiment of the present invention has been described above, it goes without saying that the present invention is not limited to the above-mentioned embodiment, and can be modified as appropriate within the scope of the gist of the present invention.

振動手段としては回転体だけでなく超音波、ポンプその
他適宜の手段を採用し得る。
As the vibration means, not only a rotating body but also ultrasonic waves, a pump, and other appropriate means can be used.

[発明の効果] 以上詳述したように本発明によれば、脱気中に液体を振
動させることによって脱気速度を速くし、しかも装置の
小型化及び低価格化を図ることかできる。
[Effects of the Invention] As described in detail above, according to the present invention, by vibrating the liquid during degassing, the degassing speed can be increased, and the device can be made smaller and less expensive.

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

第1図は、本発明に係る自動脱気装置の一実施例を示す
概略図、第2図及び第3図はそれぞれ、従来装置の概略
図である。 l・・・原液、2・・・原液容器、3・・・入口側チュ
ーブ、4・・・入口側開閉弁、5・・・脱気瓶、6・・
・脱気瓶蓋、7・・・排気チューブ、9・・・排気ポン
プ、lO・・・回転体、11.19・・・液面センサ、
12・・・出口側開閉弁、14・・・出口側チューブ、
15・・・脱気水容器、16・・・脱気水、17・・・
チューブ、18・・・圧力センサ。 代理人 弁理士 則  近  憲  協同      
大   胡   典   夫゛、I I6 第2図
FIG. 1 is a schematic diagram showing an embodiment of an automatic degassing device according to the present invention, and FIGS. 2 and 3 are schematic diagrams of conventional devices, respectively. l...Standard solution, 2...Standard solution container, 3...Inlet side tube, 4...Inlet side on/off valve, 5...Deaeration bottle, 6...
- Deaeration bottle lid, 7... Exhaust tube, 9... Exhaust pump, lO... Rotating body, 11.19... Liquid level sensor,
12... Outlet side on-off valve, 14... Outlet side tube,
15... Deaerated water container, 16... Deaerated water, 17...
Tube, 18...pressure sensor. Agent Patent Attorney Nori Chika Kyodo
Norio Ogo, I I6 Figure 2

Claims (4)

【特許請求の範囲】[Claims] (1)液体を引用にして脱気する装置において、脱気中
に液体を振動させる振動手段を設けたことを特徴とする
自動脱気装置。
(1) An automatic degassing device for degassing liquid, characterized in that it is provided with a vibration means for vibrating the liquid during degassing.
(2)前記振動手段として超音波を使用した特許請求の
範囲第1項記載の自動脱気装置。
(2) The automatic degassing device according to claim 1, wherein ultrasonic waves are used as the vibration means.
(3)前記振動手段としてマグネチックスターラを使用
した特許請求の範囲第1項記載の自動脱気装置。
(3) The automatic degassing device according to claim 1, wherein a magnetic stirrer is used as the vibration means.
(4)前記振動手段としてポンプの振動を使用した特許
請求の範囲第1項記載の自動脱気装置。
(4) The automatic degassing device according to claim 1, wherein vibration of a pump is used as the vibration means.
JP27389186A 1986-11-19 1986-11-19 Automatic deaerator Pending JPS63130107A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP27389186A JPS63130107A (en) 1986-11-19 1986-11-19 Automatic deaerator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP27389186A JPS63130107A (en) 1986-11-19 1986-11-19 Automatic deaerator

Publications (1)

Publication Number Publication Date
JPS63130107A true JPS63130107A (en) 1988-06-02

Family

ID=17534012

Family Applications (1)

Application Number Title Priority Date Filing Date
JP27389186A Pending JPS63130107A (en) 1986-11-19 1986-11-19 Automatic deaerator

Country Status (1)

Country Link
JP (1) JPS63130107A (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0271804A (en) * 1988-09-05 1990-03-12 Fujitsu Ltd Vacuum defoaming device
JPH02117003U (en) * 1989-03-01 1990-09-19
JPH0334802U (en) * 1989-08-07 1991-04-05
JPH03118892A (en) * 1989-09-29 1991-05-21 Mitsubishi Electric Corp Waste liquid treating device
EP0607984A2 (en) * 1993-01-22 1994-07-27 Sentech Corporation Method and apparatus for sampling and detecting gases in a fluid
WO2010018642A1 (en) * 2008-08-11 2010-02-18 Midori Norio Liquid deaerator

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0271804A (en) * 1988-09-05 1990-03-12 Fujitsu Ltd Vacuum defoaming device
JPH02117003U (en) * 1989-03-01 1990-09-19
JPH0334802U (en) * 1989-08-07 1991-04-05
JPH03118892A (en) * 1989-09-29 1991-05-21 Mitsubishi Electric Corp Waste liquid treating device
EP0607984A2 (en) * 1993-01-22 1994-07-27 Sentech Corporation Method and apparatus for sampling and detecting gases in a fluid
EP0607984A3 (en) * 1993-01-22 1996-07-17 Sentech Corp Method and apparatus for sampling and detecting gases in a fluid.
WO2010018642A1 (en) * 2008-08-11 2010-02-18 Midori Norio Liquid deaerator

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