JPS6353500B2 - - Google Patents
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- Publication number
- JPS6353500B2 JPS6353500B2 JP56036497A JP3649781A JPS6353500B2 JP S6353500 B2 JPS6353500 B2 JP S6353500B2 JP 56036497 A JP56036497 A JP 56036497A JP 3649781 A JP3649781 A JP 3649781A JP S6353500 B2 JPS6353500 B2 JP S6353500B2
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- JP
- Japan
- Prior art keywords
- dissolved oxygen
- sample water
- gas
- valve
- 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.)
- Expired
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Classifications
-
- G—PHYSICS
- G01—MEASURING; TESTING
- G01N—INVESTIGATING OR ANALYSING MATERIALS BY DETERMINING THEIR CHEMICAL OR PHYSICAL PROPERTIES
- G01N33/00—Investigating or analysing materials by specific methods not covered by groups G01N1/00 - G01N31/00
- G01N33/0004—Gaseous mixtures, e.g. polluted air
- G01N33/0006—Calibrating gas analysers
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- Chemical & Material Sciences (AREA)
- Life Sciences & Earth Sciences (AREA)
- Engineering & Computer Science (AREA)
- Health & Medical Sciences (AREA)
- Medicinal Chemistry (AREA)
- Food Science & Technology (AREA)
- Combustion & Propulsion (AREA)
- Physics & Mathematics (AREA)
- Analytical Chemistry (AREA)
- Biochemistry (AREA)
- General Health & Medical Sciences (AREA)
- General Physics & Mathematics (AREA)
- Immunology (AREA)
- Pathology (AREA)
- Degasification And Air Bubble Elimination (AREA)
Description
【発明の詳細な説明】
この発明は、火力・原子力発電所等において、
復・給水もしくは炉水等の溶存酸素量を連続的に
分析計測する溶存酸素分析計の校正方法に関する
ものである。[Detailed Description of the Invention] This invention provides the following advantages:
This paper relates to a method for calibrating a dissolved oxygen analyzer that continuously analyzes and measures the amount of dissolved oxygen in condensate/feed water or reactor water.
火力・原子力発電所において、復・給水系中の
溶存酸素量は、配管系等の腐蝕に対する検出要素
として重要である。このため、この種の設備にお
いては、溶存酸素量監視装置を設けて溶存酸素量
の規制を行つている。 In thermal and nuclear power plants, the amount of dissolved oxygen in the condensate and feed water systems is important as a detection element for corrosion of piping systems, etc. For this reason, in this type of equipment, a dissolved oxygen amount monitoring device is provided to regulate the amount of dissolved oxygen.
そこで、この溶存酸素量監視装置としては、主
としてポーラログラフ型式の隔膜電極を有する溶
存酸素分析計が使用されている。 Therefore, as this dissolved oxygen amount monitoring device, a dissolved oxygen analyzer having a polarographic type diaphragm electrode is mainly used.
ところで、この種の溶存酸素分析計は、試料水
中に酸素が存在すると、両電極間の電位差に対す
るポーラログラフイーの酸素曲線に従つて電流が
流れ、しかもこの電流量は試料水中の酸素分圧に
比例するものである。また、この種の溶存酸素分
析計を使用する場合、その動作特性上校正が必要
であり、この校正方法として一般にフアラデーセ
ルを使用する等の既知量増加法が適用されてい
る。すなわち、既知量増加法とは、試料水中に既
知量の酸素を添加する方式であり、この既知量の
酸素の添加手段として、試料水を電気分解して陽
極反応で酸素を発生させるよう構成する。従つ
て、前記電気分解による陽極反応で発生する酸素
量は、電流効率を100%とすれば、電流値より知
ることができる。 By the way, in this type of dissolved oxygen analyzer, when oxygen exists in the sample water, a current flows according to the polarographic oxygen curve with respect to the potential difference between the two electrodes, and the amount of current is proportional to the oxygen partial pressure in the sample water. It is something to do. Further, when using this type of dissolved oxygen analyzer, calibration is required due to its operating characteristics, and a known quantity increase method, such as using a Faraday cell, is generally used as a calibration method. In other words, the known amount increase method is a method in which a known amount of oxygen is added to the sample water, and as a means for adding this known amount of oxygen, the sample water is electrolyzed and oxygen is generated by an anode reaction. . Therefore, the amount of oxygen generated in the anodic reaction caused by electrolysis can be known from the current value, assuming that the current efficiency is 100%.
しかしながら、前述した従来の溶存酸素分析計
の校正方式によれば、起動時等のように試料水中
の溶存酸素量が飽和状態(6〜8ppm)にある場
合には、試料水中の溶存酸素量が不明確となるた
め、校正が不能である。一方、起動後運転に入つ
た場合、通常10〜100ppbの微量酸素を正確に計
測するために校正を行う際には、別途に既知の微
量酸素量の校正液を作成して分析計電極に導入す
る必要がある。しかし、既知の微量溶存酸素量の
校正液を作成することは事実上不可能であるた
め、運転後に校正を行わざるを得ず、このため従
来の溶存酸素分析計においては起動直後の溶存酸
素量計測値の信頼性がきわめて低いものであつ
た。 However, according to the calibration method of the conventional dissolved oxygen analyzer mentioned above, when the amount of dissolved oxygen in the sample water is in a saturated state (6 to 8 ppm), such as at startup, the amount of dissolved oxygen in the sample water is Calibration is not possible because it is unclear. On the other hand, when starting operation after startup, when performing calibration to accurately measure trace oxygen, usually 10 to 100 ppb, separately prepare a calibration solution with a known trace oxygen amount and introduce it into the analyzer electrode. There is a need to. However, since it is virtually impossible to create a calibration solution with a known trace amount of dissolved oxygen, calibration must be performed after operation. The reliability of the measured values was extremely low.
そこで、本発明者等は、前述した従来の溶存酸
素分析計の校正方式における問題点を全て克服す
べく種々検討並びに試作を重ねた結果、所定容量
の脱気槽を設け、起動時等の高濃度溶存酸素量の
試料水を脱気槽に所定量導入し、次いで脱気槽内
の底部および中位部より不活性ガスを放出して試
料水を所定時間バブリングし、脱気槽内の試料水
中の溶存酸素を外部へ排気して微量溶存酸素量と
し、その後脱気槽内の試料水を不活性ガスの圧力
下にフアラデーセルおよび溶存酸素分析計を含む
分析系へ供給することにより、フアラデーセルに
よる校正を適正に行うことができ、前記問題点を
一挙に解消し得ることを突き止めた。 Therefore, the present inventors conducted various studies and made prototypes in order to overcome all the problems in the conventional calibration method of dissolved oxygen analyzers mentioned above. As a result, the present inventors installed a degassing tank with a predetermined capacity and set up a degassing tank with a specified capacity. A predetermined amount of sample water with a concentration of dissolved oxygen is introduced into the deaeration tank, and then an inert gas is released from the bottom and middle part of the deaeration tank to bubble the sample water for a predetermined time. Dissolved oxygen in the water is exhausted to the outside to reduce the amount of dissolved oxygen, and then the sample water in the degassing tank is supplied to the analysis system including the Faraday cell and dissolved oxygen analyzer under the pressure of inert gas. It has been found that calibration can be performed properly and that the above problems can be solved at once.
なお、前記脱気槽において、試料水のバブリン
グを最も効果的に行うには、多孔質の焼結金属ま
たはセラミツクで構成した散気管を脱気槽の中心
部より放射状に配設し、しかも一部の散気管は放
出量を調節可能に構成すれば好適であることが判
つた。なお、脱気槽は、起動時等において、前述
したように一時的に使用し、校正が終了したら試
料水配管から分離して試料水を直接前記分析計に
導入するよう配管接続すれば、溶存酸素分析計の
校正はフアラデーセルのみで適正かつ円滑に達成
することができる。 In order to most effectively bubble the sample water in the deaeration tank, diffuser tubes made of porous sintered metal or ceramic should be arranged radially from the center of the deaeration tank, and It has been found that it is preferable to configure the air diffuser tube in the section so that the amount of discharge can be adjusted. Note that the deaeration tank can be used temporarily as mentioned above, such as during startup, and after calibration is completed, it can be separated from the sample water piping and connected to the piping to directly introduce the sample water into the analyzer. Calibration of an oxygen analyzer can be accomplished properly and smoothly using only a Faraday cell.
従つて、本発明の目的は、試料水配管に流量計
および流量調整弁を設け、フアラデーセル等を介
して溶存酸素分析計を接続してなる試料水の溶存
酸素分析系において、起動時等における溶存酸素
量が高濃度となる試料水に対し、試料水の溶存酸
素量の低減を円滑かつ簡便に行うと共に既知量増
加法による溶存酸素分析計の校正を適正に行うこ
とができる校正方式を提供するにある。 Therefore, it is an object of the present invention to detect dissolved oxygen during startup, etc. in a sample water dissolved oxygen analysis system in which a flow meter and a flow rate adjustment valve are installed in sample water piping, and a dissolved oxygen analyzer is connected via a Faraday cell or the like. To provide a calibration method that can smoothly and easily reduce the amount of dissolved oxygen in a sample water with a high concentration of oxygen, and can properly calibrate a dissolved oxygen analyzer using a known amount increase method. It is in.
前記の目的を達成するため、本発明において
は、試料水配管に元弁、流量調整弁、流量計およ
びフアラデーセルを介して溶存酸素分析計を接続
配置すると共に既知量増加法により前記溶存酸素
分析計の校正を行うよう構成した溶存酸素分析装
置において、
前記試料水配管の元弁の上流側と下流側にそれ
ぞれ入口弁と出口弁を介して試料水を導出する配
管を接続すると共にこれら配管を脱気槽に連通接
続し、
前記脱気槽に対し不活性ガス供給源と連通する
ガス配管を導入すると共にこのガス配管の一部に
切換弁を設けてこれを2方に分岐し、一方の分岐
ガス配管を脱気槽の底部内に延在させてその先端
部に放射状に延在する複数の散気管を設け、他方
の分岐ガス配管を脱気槽の内部上方に開口し、
脱気処理工程において前記他方の分岐ガス配管
より不活性ガスを脱気槽の内部上方に導入して内
部気体をパージした後前記一方の分岐ガス配管よ
り不活性ガスを試料水中に噴射して溶存酸素をパ
ージして脱気処理を行い、次いで前記他方の分岐
ガス配管より不活性ガスを導入しながら前記出口
弁を開放して脱気槽内のガス圧力と脱気水の水頭
により脱気試料水を溶存酸素分析計に対し供給す
ることを特徴とする。 In order to achieve the above object, in the present invention, a dissolved oxygen analyzer is connected to the sample water piping via a main valve, a flow rate adjustment valve, a flow meter, and a Faraday cell, and the dissolved oxygen analyzer is In a dissolved oxygen analyzer configured to perform calibration, pipes for leading out sample water are connected to the upstream and downstream sides of the main valve of the sample water pipe through an inlet valve and an outlet valve, respectively, and these pipes are disconnected. A gas pipe is connected to the deaeration tank and communicated with an inert gas supply source to the deaeration tank, and a switching valve is provided in a part of this gas pipe to branch it into two directions, one branch being connected to the other. The gas pipe is extended into the bottom of the deaeration tank, a plurality of radially extending aeration pipes are provided at the tip thereof, and the other branch gas pipe is opened upward inside the deaeration tank to perform the deaeration process. After introducing an inert gas into the upper part of the degassing tank from the other branch gas pipe to purge the internal gas, inject the inert gas into the sample water from the one branch gas pipe to purge dissolved oxygen. Then, the outlet valve is opened while introducing an inert gas from the other branch gas pipe, and the degassed sample water is degassed with dissolved oxygen by the gas pressure in the degassing tank and the head of the degassed water. It is characterized by being supplied to an analyzer.
前記の校正方法において、散気管は、多孔質の
焼結金属またはセラミツクからなり、先端部を閉
塞した中空間で構成し、さらに脱気槽内に延在す
る分岐ガス配管の中位部に放射状に延在する可調
整散気管を設ければ好適である。 In the calibration method described above, the diffuser tube is made of porous sintered metal or ceramic, has a hollow space with a closed end, and is radially connected to the middle part of the branch gas pipe extending into the degassing tank. It is preferable to provide an adjustable air diffuser pipe that extends to.
また、脱気槽の頂部に脱気用ベント管を設ける
と共に内部異常過圧保護用の逃し弁を設ければ好
適である。 Further, it is preferable to provide a vent pipe for deaeration at the top of the deaeration tank and a relief valve for protection against internal abnormal overpressure.
次に、本発明に係る溶存酸素分析計校正方式の
実施例につきフアラデーセルを使用する既知量増
加法を例示して以下添付図面を参照しながら詳細
に説明する。 Next, an embodiment of the dissolved oxygen analyzer calibration method according to the present invention will be described in detail with reference to the accompanying drawings, illustrating a known quantity increase method using a Faraday cell.
第1図は、本発明方式の一実施例を示す系統図
である。すなわち、第1図において、参照符号1
0は試料水供給配管、12は試料水元弁、14は
流量調整弁、16は流量計、18はフアラデーセ
ル、20は溶存酸素分析計をそれぞれ示す。しか
るに、前記試料水元弁12を開放し、流量調整弁
14および流量計16により試料水の流量を調整
しながらフアラデーセル18を介して溶存酸素分
析計20に試料水を供給することにより、試料水
の連続的な計測を行うことができるよう構成され
ている。以上の構成からなる分析系は従来の溶存
酸素分析計と基本的に同一である。 FIG. 1 is a system diagram showing an embodiment of the system of the present invention. That is, in FIG.
0 is a sample water supply pipe, 12 is a sample water source valve, 14 is a flow rate adjustment valve, 16 is a flow meter, 18 is a Faraday cell, and 20 is a dissolved oxygen analyzer. However, by opening the sample water source valve 12 and supplying the sample water to the dissolved oxygen analyzer 20 via the Faraday cell 18 while adjusting the flow rate of the sample water using the flow rate adjustment valve 14 and the flow meter 16, the sample water It is configured to be able to perform continuous measurements. The analysis system having the above configuration is basically the same as a conventional dissolved oxygen analyzer.
そこで、本発明においては、前記試料水供給配
管10に接続配置した試料水元弁12の上流側と
下流側とからそれぞれ入口弁22および出口弁2
4を介して試料水入口配管26および試料水出口
配管28を導出し、これらの入口配管26および
出口配管28を脱気槽30に連通接続する。脱気
槽30は、一般に円筒形に構成された密閉容器か
らなり、上側面部に入口配管26を連通すると共
に下側面部に出口配管28を連通し、一側面部に
は適宜元弁32を介して液面計34を設ける。ま
た、脱気槽30の頂部には開閉蓋36が着脱自在
に設けられ、この開閉蓋36の中心部より脱気槽
30内へ垂直に散気用ガス配管38を挿通配置
し、その下端部を放射状に配設した複数本の散気
管40にそれぞれ連通する(第2図参照)。また、
前記ガス配管38の脱気槽30内の中位部におい
て、適宜調整弁42を介して放出ガス量を調整し
得る可調整散気管44を、前記散気管40と重な
らないよう放射状に接続配置する(第3図参照)。
なお、本実施例において使用する散気管40,4
4としては、多孔質の焼結金属またはセラミツク
で構成し、先端部を閉塞した中空管構造のものが
好適である。 Therefore, in the present invention, an inlet valve 22 and an outlet valve 2 are provided from the upstream side and the downstream side of the sample water source valve 12 connected to the sample water supply pipe 10, respectively.
4, a sample water inlet pipe 26 and a sample water outlet pipe 28 are led out, and these inlet pipe 26 and outlet pipe 28 are connected to a degassing tank 30. The deaeration tank 30 is generally a cylindrical sealed container, has an inlet pipe 26 connected to its upper side, an outlet pipe 28 connected to its lower side, and has a main valve 32 connected to one side as appropriate. A liquid level gauge 34 is provided therebetween. Further, an opening/closing lid 36 is detachably provided at the top of the deaeration tank 30, and a gas pipe 38 for aeration is inserted vertically into the deaeration tank 30 from the center of the opening/closing lid 36, and the lower end thereof is inserted into the deaeration tank 30 vertically. are connected to a plurality of air diffusers 40 arranged radially (see FIG. 2). Also,
In the middle part of the gas pipe 38 in the deaeration tank 30, adjustable aeration pipes 44 capable of adjusting the amount of released gas via an adjustment valve 42 are radially connected and arranged so as not to overlap with the aeration pipe 40. (See Figure 3).
Note that the diffuser pipes 40, 4 used in this example
4 is preferably made of porous sintered metal or ceramic and has a hollow tube structure with a closed tip.
脱気槽30の開閉蓋36には、ベント弁46を
介してパージガスを排気するためのベント管48
を接続配置すると共に異常過圧に対する保護のた
めの逃し弁50を接続配置する。また、前記開閉
蓋36の中心部に挿通配置したガス配管38は、
第1図に示すように、三方切換弁52、ガス流量
調整弁54、圧力調整弁56およびボンベ元弁5
8をそれぞれ介して不活性ガスボンベ60に連通
接続する。なお、前記圧力調整弁56の前後には
それぞれ一次圧力計62および二次圧力計64を
設けて圧力調整を容易になし得るようにする。ま
た、前記三方切換弁52から導出するバイパス管
66は、前記開閉蓋36を介して脱気槽30の頂
部内に開口するノズル68に連通接続する。さら
に、脱気槽30の底部には、ドレン弁70を介し
て残留試料水を排出するためのドレン管72を設
ける。 The opening/closing lid 36 of the deaeration tank 30 is provided with a vent pipe 48 for exhausting purge gas via a vent valve 46.
A relief valve 50 for protection against abnormal overpressure is also connected and arranged. Further, the gas pipe 38 inserted through the center of the opening/closing lid 36 is
As shown in FIG. 1, a three-way switching valve 52, a gas flow rate adjustment valve 54, a pressure adjustment valve 56, and a cylinder main valve 5
8, respectively, to an inert gas cylinder 60. A primary pressure gauge 62 and a secondary pressure gauge 64 are provided before and after the pressure regulating valve 56, respectively, to facilitate pressure regulation. Further, a bypass pipe 66 led out from the three-way switching valve 52 is connected to a nozzle 68 that opens into the top of the degassing tank 30 via the opening/closing lid 36. Furthermore, a drain pipe 72 is provided at the bottom of the deaeration tank 30 for discharging residual sample water via a drain valve 70.
次に、前述した構成からなる脱気槽30を使用
して、溶存酸素分析計20に対する校正を行う場
合の手順につきその作用との関係において説明す
る。 Next, a procedure for calibrating the dissolved oxygen analyzer 20 using the degassing tank 30 having the above-described configuration will be described in relation to its operation.
1 起動時における脱気槽への試料水導入操作
まず、試料水元弁12と出口弁24を閉塞す
ると共に入口弁22およびベント弁46を開放
して、起動時の試料水を入口配管26を介して
脱気槽30に導入する。この場合、脱気槽30
の全体容積は約56に設定し、試料水を約50
連続的に導入すれば好適である。脱気槽30
に所定量の試料水が導入されたことを液面計3
4で確認して入口弁22を閉塞する。1 Operation for introducing sample water into the deaeration tank at startup First, close the sample water source valve 12 and outlet valve 24, open the inlet valve 22 and vent valve 46, and introduce the sample water at startup into the inlet pipe 26. The gas is introduced into the deaeration tank 30 through the air. In this case, the deaeration tank 30
The total volume of the sample water is set to about 56, and the sample water is about 50
It is preferable to introduce it continuously. Deaeration tank 30
Level gauge 3 indicates that a predetermined amount of sample water has been introduced.
4 and close the inlet valve 22.
2 試料水の脱気処理操作
まず、ガス配管38に接続された三方切換弁
52をバイパス管66と連通するよう操作した
後、ボンベ元弁58を開放し、例えば窒素ガス
等の不活性ガスを所定圧(1.4Kg/cm2)に保持
してノズル68から脱気槽30内の気相部分へ
供給し、ベンド管48を介して試料水導入時の
気相側の酸素をパージする。2 Degassing operation of sample water First, after operating the three-way switching valve 52 connected to the gas pipe 38 to communicate with the bypass pipe 66, the cylinder main valve 58 is opened and an inert gas such as nitrogen gas is introduced. The sample water is maintained at a predetermined pressure (1.4 kg/cm 2 ) and supplied from the nozzle 68 to the gas phase portion of the degassing tank 30, and the oxygen in the gas phase when the sample water is introduced is purged through the bend pipe 48.
次いで、三方切換弁52を切換えて、散気管
40から試料水中に不活性ガスを噴射する。こ
の場合、散気管40は多孔質の焼結金属または
セラミツクで構成したため、試料水中への噴射
ガスは極めて細かい気泡となつて気液接触面が
拡大され、溶存酸素のパージを効率よく達成す
ることができる。また、可調整散気管44によ
り噴射ガス量を適宜調整することにより、脱気
槽30内における気相中の分圧を変化させて、
試料水中の溶存酸素量を調整することができ
る。因みに、不活性ガスの供給圧力を1.4Kg/
cm2とした場合、散気管40のみを使用する際に
は約30分の脱気処理で溶存酸素量を10ppbにす
ることができるのに対し、可調整散気管44を
全開にして併用する際には同一条件で溶存酸素
量を3ppbにすることができる。 Next, the three-way switching valve 52 is switched to inject inert gas into the sample water from the aeration pipe 40. In this case, since the diffuser tube 40 is made of porous sintered metal or ceramic, the gas injected into the sample water becomes extremely fine bubbles, expanding the gas-liquid contact surface and efficiently purging dissolved oxygen. I can do it. In addition, by appropriately adjusting the amount of injected gas using the adjustable air diffuser 44, the partial pressure in the gas phase in the degassing tank 30 can be changed,
The amount of dissolved oxygen in sample water can be adjusted. By the way, the inert gas supply pressure is 1.4Kg/
cm 2 , when using only the air diffuser 40, the amount of dissolved oxygen can be reduced to 10 ppb with about 30 minutes of deaeration treatment, whereas when the adjustable air diffuser 44 is fully opened and used together. The amount of dissolved oxygen can be reduced to 3 ppb under the same conditions.
3 脱気処理後の試料水の供給並びに校正操作
前記の脱気処理工程が終了すると、出口弁2
4を開放し、脱気槽30内へ三方切換弁52を
介してバイパス管66およびノズル68から導
入される不活性ガスの圧力下および脱気試料水
の水頭により脱気試料水を分析系へ供給する。3 Supply of sample water after degassing treatment and calibration operation When the degassing treatment process described above is completed, the outlet valve 2
4 is opened, and the degassed sample water is introduced into the analysis system under the pressure of the inert gas introduced into the degassing tank 30 from the bypass pipe 66 and nozzle 68 via the three-way switching valve 52 and by the water head of the degassed sample water. supply
このようにして、分析系へ供給された試料水
は、フアラデーセル18で10〜30ppbの溶存酸
素を発生させれば、低濃度溶存酸素域の13〜
33ppbの範囲内において溶存酸素分析計20の
校正を行うことができる。 In this way, if the sample water supplied to the analysis system generates dissolved oxygen of 10 to 30 ppb in the Faraday cell 18, the sample water is in the low concentration dissolved oxygen range of 13 to
The dissolved oxygen analyzer 20 can be calibrated within the range of 33 ppb.
4 校正作業後の操作
前述の校正作業が終了した場合は、不活性ガ
スボンベ60の元弁58および出口弁24を閉
塞して脱気槽30を分析系から分離すると共に
試料水元弁12を開放し、試料水供給配管10
より試料水を直接分析系へ供給して試料水の連
続測定を行う。また、脱気槽30内に残留した
脱気試料水は、ドレン弁70を開放し、ドレン
管72を介して外部へ放出し、次の起動時等に
おける分析計の校正作業に備える。4 Operations after calibration work When the above-mentioned calibration work is completed, close the main valve 58 and outlet valve 24 of the inert gas cylinder 60 to separate the deaeration tank 30 from the analysis system, and open the sample water main valve 12. and sample water supply piping 10
The sample water is directly supplied to the analysis system and the sample water is continuously measured. Further, the degassed sample water remaining in the deaeration tank 30 is released to the outside through the drain pipe 72 by opening the drain valve 70, in preparation for the calibration work of the analyzer at the next startup, etc.
前述した実施例から明らかなように、本発明に
よれば、起動時等において溶存酸素量が飽和状態
となる試料水を予め脱気槽へ回収して一定の微量
溶存酸素量の試料水とすることができ、しかもこ
の場合に溶存酸素をパージするために使用した不
活性ガスの圧力で脱気槽から分析系へ脱気試料水
を供給し、フアラデーセルによる溶存酸素分析計
の校正を適正に行うことができる。 As is clear from the embodiments described above, according to the present invention, sample water whose dissolved oxygen content reaches a saturated state at the time of startup etc. is collected in advance into a deaeration tank to obtain sample water with a constant trace amount of dissolved oxygen. In this case, the degassed sample water can be supplied from the deaeration tank to the analysis system using the pressure of the inert gas used to purge dissolved oxygen, and the dissolved oxygen analyzer can be properly calibrated using the Faraday cell. be able to.
また、本発明に使用する脱気槽は、構成が極め
て簡単であり、入口弁と出口弁の操作により試料
水供給系と分析系との間に連通接続し、試料水の
脱気処理を効率よくしかも可調整に達成すること
ができる。特に、脱気処理操作および脱気試料水
の供給操作に際し、モータおよびポンプ等の駆動
手段を使用することなく、不活性ガスの圧力で簡
便に操作することができるので、取扱い並びに保
守管理等も容易である等の利点を有する。 Furthermore, the deaeration tank used in the present invention has an extremely simple configuration, and can be connected between the sample water supply system and the analysis system by operating the inlet and outlet valves, allowing for efficient deaeration of the sample water. This can be achieved well and tunably. In particular, when degassing and supplying degassed sample water, it can be easily operated using inert gas pressure without using drive means such as motors and pumps, making handling and maintenance easier. It has advantages such as being easy to use.
以上、本発明の好適な実施例について説明した
が、本発明の精神を逸脱しない範囲内において
種々の設計変更をなし得ることは勿論である。 Although the preferred embodiments of the present invention have been described above, it goes without saying that various design changes can be made without departing from the spirit of the present invention.
第1図は本発明に係る溶存酸素分析計の校正方
式の一実施例を示す系統図、第2図は本発明方式
に使用する脱気槽の断面説明図、第3図は第2図
に示す散気管の取付状態を示す平面図である。
10……試料水供給配管、12……試料水元
弁、14……流量調節弁、16……流量計、18
……フアラデーセル、20……溶存酸素分析計、
22……入口弁、24……出口弁、26……入口
配管、28……出口配管、30……脱気槽、32
……元弁、34……液面計、36……開閉蓋、3
8……ガス配管、40……散気管、42……調整
弁、44……可調整散気管、46……ベント弁、
48……ベント管、50……逃し弁、52……三
方切換弁、54……ガス流量調整弁、56……圧
力調整弁、58……ボンベ元弁、60……不活性
ガスボンベ、62……一次圧力計、64……二次
圧力計、66……バイパス管、68……ノズル、
70……ドレン弁、72……ドレン管。
Fig. 1 is a system diagram showing one embodiment of the calibration method for a dissolved oxygen analyzer according to the present invention, Fig. 2 is a cross-sectional explanatory diagram of a degassing tank used in the method of the present invention, and Fig. 3 is similar to Fig. 2. It is a top view which shows the attachment state of the air diffuser shown in FIG. 10... Sample water supply piping, 12... Sample water source valve, 14... Flow rate adjustment valve, 16... Flow meter, 18
... Farade cell, 20 ... Dissolved oxygen analyzer,
22... Inlet valve, 24... Outlet valve, 26... Inlet piping, 28... Outlet piping, 30... Deaeration tank, 32
... Main valve, 34 ... Liquid level gauge, 36 ... Opening/closing lid, 3
8...Gas piping, 40...Diffuser pipe, 42...Adjustment valve, 44...Adjustable air diffuser pipe, 46...Vent valve,
48... Vent pipe, 50... Relief valve, 52... Three-way switching valve, 54... Gas flow rate adjustment valve, 56... Pressure adjustment valve, 58... Cylinder main valve, 60... Inert gas cylinder, 62... ...Primary pressure gauge, 64...Secondary pressure gauge, 66...Bypass pipe, 68...Nozzle,
70...Drain valve, 72...Drain pipe.
Claims (1)
びフアラデーセルを介して溶存酸素分析計を接続
配置すると共に既知量増加法により前記溶存酸素
分析計の校正を行うよう構成した溶存酸素分析装
置において、 前記試料水配管の元弁の上流側と下流側にそれ
ぞれ入口弁と出口弁を介して試料水を導出する配
管を接続すると共にこれら配管を脱気槽に連通接
続し、 前記脱気槽に対し不活性ガス供給源と連通する
ガス配管を導入すると共にこのガス配管の一部に
切換弁を設けてこれを2方に分岐し、一方の分岐
ガス配管を脱気槽の底部内に延在させてその先端
部に放射状に延在する複数の散気管を設け、他方
の分岐ガス配管を脱気槽の内部上方に開口し、 脱気処理工程において前記他方の分岐ガス配管
より不活性ガスを脱気槽の内部上方に導入して内
部気体をパージした後前記一方の分岐ガス配管よ
り不活性ガスを試料水中に噴射して溶存酸素をパ
ージして脱気処理を行い、次いで前記他方の分岐
ガス配管より不活性ガスを導入しながら前記出口
弁を開放して脱気槽内のガス圧力と脱気水の水頭
により脱気試料水を溶存酸素分析計に対し供給す
ることを特徴とする溶存酸素分析計の校正方法。 2 特許請求の範囲第1項記載の溶存酸素分析計
の校正方法において、 散気管は、多孔質の焼結金属またはセラミツク
からなり、先端部を閉塞した中空管で構成し、さ
らに脱気槽内に延在する分岐ガス配管の中位部に
放射状に延在する可調整散気管を設けてなる溶存
酸素分析計の校正方法。 3 特許請求の範囲第1項記載の溶存酸素分析計
の校正方法において、 脱気槽の頂部に脱気用ベント管を設けると共に
内部異常過圧保護用の逃し弁を設けてなる特許請
求の範囲第1項記載の溶存酸素分析計の校正方
法。[Scope of Claims] 1. A dissolved oxygen analyzer is connected to the sample water piping via a main valve, a flow rate adjustment valve, a flow meter, and a Faraday cell, and the dissolved oxygen analyzer is calibrated by a known amount increase method. In the dissolved oxygen analyzer, pipes for extracting sample water are connected to the upstream and downstream sides of the main valve of the sample water pipe through an inlet valve and an outlet valve, respectively, and these pipes are connected to a degassing tank. , A gas pipe communicating with an inert gas supply source is introduced into the deaeration tank, and a switching valve is provided in a part of this gas pipe to branch it into two directions, and one branched gas pipe is connected to the deaeration tank. A plurality of aeration pipes are provided extending in the bottom of the tank and extending radially at the tips thereof, and the other branch gas pipe is opened upwardly inside the deaeration tank, and the other branch gas is removed in the deaeration treatment process. After introducing an inert gas into the upper part of the degassing tank through the piping to purge the internal gas, inject the inert gas into the sample water from one of the branched gas piping to purge dissolved oxygen and perform the degassing process. Then, while introducing an inert gas from the other branch gas pipe, open the outlet valve and supply degassed sample water to the dissolved oxygen analyzer using the gas pressure in the degassing tank and the head of the degassed water. A method for calibrating a dissolved oxygen analyzer, characterized in that: 2. In the method for calibrating a dissolved oxygen analyzer according to claim 1, the aeration tube is a hollow tube made of porous sintered metal or ceramic and has a closed tip, and further includes a degassing tank. A method for calibrating a dissolved oxygen analyzer in which an adjustable air diffuser pipe that extends radially is provided in the middle part of a branch gas pipe that extends within the interior. 3. In the method for calibrating a dissolved oxygen analyzer as set forth in claim 1, a deaeration vent pipe is provided at the top of the deaeration tank, and a relief valve is provided to protect against internal abnormal overpressure. A method for calibrating a dissolved oxygen analyzer according to paragraph 1.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3649781A JPS57151847A (en) | 1981-03-16 | 1981-03-16 | Calibration system for dissolved oxygen analyser |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3649781A JPS57151847A (en) | 1981-03-16 | 1981-03-16 | Calibration system for dissolved oxygen analyser |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS57151847A JPS57151847A (en) | 1982-09-20 |
| JPS6353500B2 true JPS6353500B2 (en) | 1988-10-24 |
Family
ID=12471457
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP3649781A Granted JPS57151847A (en) | 1981-03-16 | 1981-03-16 | Calibration system for dissolved oxygen analyser |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS57151847A (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS59213411A (en) * | 1983-05-17 | 1984-12-03 | Tatsuo Okazaki | Apparatus for removing carbon dioxide in water |
| CN103245533B (en) * | 2013-05-02 | 2015-09-02 | 中国科学院合肥物质科学研究院 | The water sample acquisition device of heavy metal online analyzer in a kind of water |
| CN105424769B (en) * | 2015-11-09 | 2018-10-26 | 北京华科仪科技股份有限公司 | A kind of trace dissolved oxygen analyzer on-line calibration device and its calibration method |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5622947A (en) * | 1979-06-27 | 1981-03-04 | Toshiba Corp | Analyzer for dissolved oxygen |
-
1981
- 1981-03-16 JP JP3649781A patent/JPS57151847A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS57151847A (en) | 1982-09-20 |
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