JPH0618474A - Batch continuous method for measuring ammonia in water - Google Patents
Batch continuous method for measuring ammonia in waterInfo
- Publication number
- JPH0618474A JPH0618474A JP4177255A JP17725592A JPH0618474A JP H0618474 A JPH0618474 A JP H0618474A JP 4177255 A JP4177255 A JP 4177255A JP 17725592 A JP17725592 A JP 17725592A JP H0618474 A JPH0618474 A JP H0618474A
- Authority
- JP
- Japan
- Prior art keywords
- ammonia
- water
- sample water
- measuring
- concentration
- 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
Links
Landscapes
- Investigating Or Analyzing Non-Biological Materials By The Use Of Chemical Means (AREA)
Description
【0001】[0001]
【産業上の利用分野】本発明は、水に含まれるアンモニ
ア性窒素の濃度をオンラインで測定するバッチ連続式水
中アンモニア測定方法に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a batch continuous water ammonia measuring method for on-line measuring the concentration of ammonia nitrogen contained in water.
【0002】[0002]
【従来の技術】生物学的脱窒プロセスではプロセスを監
視するために、処理水中のアンモニア性窒素(以下NH
3 −Nという)の濃度を測定する必要がある。一方、浄
水場では原水の汚染の指標としてNH3 −Nの重要性が
知られている。このような点からNH3 −N濃度の測
定、特にオンラインで長期にわたり、自動分析が可能な
装置に対する必要性が指摘されている。2. Description of the Related Art In a biological denitrification process, in order to monitor the process, ammoniacal nitrogen (hereinafter referred to as NH
It is necessary to measure the concentration of ( 3- N). On the other hand, the importance of NH 3 —N is known as an index of pollution of raw water in water purification plants. From this point of view, it is pointed out that there is a need for an apparatus capable of measuring NH 3 —N concentration, particularly on-line for a long time and automatically analyzing.
【0003】上記のような必要性を満たすために、本出
願人の提案による特開昭63−165751号にて水中
アンモニアの分析方法が公知である。上記の先願発明の
要旨は次記の通りである。測定セル内に気相部を形成し
て試料水を通流させ、この試料水にアルカリを加えてp
H11以上にしてNH3 −Nを溶存アンモニアガスとし
て存在させる。そして測定セル内の試料水を緩かに攪拌
する。この場合、気相部のアンモニアガス濃度は試料水
中のNH3 −N濃度に比例するので、気相部のアンモニ
アガスをアンモニアガス電極で検知し、そのとき得られ
る出力から試料水のNH3 −N濃度を求める。In order to meet the above needs, a method for analyzing ammonia in water is known from Japanese Patent Laid-Open No. 63-165751 proposed by the present applicant. The gist of the above-mentioned prior invention is as follows. A gas phase is formed in the measuring cell to let the sample water flow, and an alkali is added to this sample water to add p.
After H11 or more, NH 3 —N is present as dissolved ammonia gas. Then, the sample water in the measurement cell is gently stirred. In this case, since the ammonia gas concentration in the gas phase portion is proportional to the NH 3 -N concentration in the sample water, the ammonia gas electrode in the gas phase portion is detected by the ammonia gas electrode, and the NH 3- Determine the N concentration.
【0004】この際既知のアンモニア濃度を有する標準
溶液の試料水への混入率を一定周期で変化させつつ、混
入率切換周期の整数倍に相当する時間にわたるアンモニ
アガス電極出力の移動平均と、移動平均時間の1/2に
相当する時間だけ過去のアンモニアガス電極出力値を用
いて試料水中のNH3 −N濃度を求めている。At this time, while changing the mixing ratio of the standard solution having a known ammonia concentration into the sample water at a constant cycle, the moving average and the moving average of the ammonia gas electrode output over a time corresponding to an integral multiple of the mixing ratio switching cycle are changed. The NH 3 —N concentration in the sample water is obtained by using the past ammonia gas electrode output value for a time corresponding to ½ of the average time.
【0005】[0005]
【発明が解決しようとする課題】上記のような水中アン
モニア測定方法では連続通流式であるために、常時アル
カリが注入され、標準溶液が混入されることになり、 薬品使用量が多くなり、特にアルカリと反応して生じ
るスケールが配管内に蓄積されて配管が閉塞される恐れ
がある。Since the above-mentioned method for measuring ammonia in water is of the continuous flow type, alkali is always injected and the standard solution is mixed, resulting in a large amount of chemicals used. In particular, the scale generated by the reaction with alkali may be accumulated in the pipe and the pipe may be blocked.
【0006】標準溶液の混入精度に測定機器の精度が
追従できないため、安定性に欠ける。 排液量が多くなる。 アンモニアガス電極の出力の安定化まで時間がかか
る。 応答が遅く、急激な濃度に変化に対応できない。 等の問題点がある。Since the precision of the measuring instrument cannot follow the precision of mixing the standard solution, it lacks stability. The amount of drainage increases. It takes time to stabilize the output of the ammonia gas electrode. The response is slow, and it is not possible to respond to sudden changes in concentration. There are problems such as.
【0007】上記の問題点を解決するために本出願人は
特開平3−61856号にてバッチ連続式自動アンモニ
ア測定方法を提案したが、さらに別の方法について提案
する。本発明の目的は、応答時間が短縮され、薬品の使
用量が減少し、メンテナンスが容易で、長期間安定した
測定が可能なバッチ連続式水中アンモニア測定方法を提
供する。In order to solve the above problems, the present applicant proposed a batch continuous automatic ammonia measuring method in Japanese Patent Laid-Open No. 3-61856, but proposes another method. An object of the present invention is to provide a batch continuous ammonia measuring method for water, which has a short response time, a small amount of chemicals, is easy to maintain, and can be stably measured for a long period of time.
【0008】[0008]
【課題を解決するための手段】上記課題を解決するため
に、本発明によればバッチ連続式水中アンモニア測定方
法は、恒温槽に収納された測定セル内に気相部を形成し
て一定量の試料水を注水し、同時にアルカリを加えてp
H11以上にした後、試料水を一定温度に保持して攪拌
し、試料水中のアンモニアをガス化して気相部に移行さ
せ、この気相部のアンモニアガスを隔膜式アンモニアガ
ス電極で検知して得られた出力からあらかじめ作製する
検量線に基づいて試料水中のアンモニア濃度を定量する
ものとする。In order to solve the above-mentioned problems, according to the present invention, a batch continuous type ammonia measuring method according to the present invention forms a gas phase part in a measuring cell housed in a constant temperature bath to form a constant amount. Pour the sample water of, and at the same time add alkali
After making H11 or more, the sample water is kept at a constant temperature and stirred, the ammonia in the sample water is gasified and transferred to the gas phase part, and the ammonia gas in this gas phase part is detected by the diaphragm type ammonia gas electrode. The ammonia concentration in the sample water shall be quantified based on the calibration curve prepared in advance from the obtained output.
【0009】[0009]
【作用】バッチ式に測定セル内に気相部を形成して注入
される一定量の試料水にアルカリを加えてpH11以上
にすることにより、試料水中のアンモニアは溶存アンモ
ニアガスとして存在する。この状態で試料水を一定温度
に保って攪拌すれば溶存アンモニアはガス化されて気相
部に移行する。したがって気相部に移行したアンモニア
ガスを隔膜式アンモニアガス電極により検知して電極出
力が得られる。Ammonia in the sample water exists as dissolved ammonia gas by adding an alkali to a fixed amount of the sample water injected by forming a gas phase portion in the measuring cell in a batch method to adjust the pH to 11 or more. In this state, if the sample water is kept at a constant temperature and stirred, the dissolved ammonia is gasified and transferred to the gas phase part. Therefore, the ammonia gas transferred to the gas phase portion is detected by the diaphragm type ammonia gas electrode to obtain the electrode output.
【0010】そうして、あらかじめ検量線を求めておく
ことにより、この検量線に基づいて前記電極出力から試
料水中のアンモニア濃度を定量することができる。By thus obtaining the calibration curve in advance, it is possible to quantify the ammonia concentration in the sample water from the electrode output based on this calibration curve.
【0011】[0011]
【実施例】以下図面に基づいて本発明の実施例によるバ
ッチ連続式水中アンモニア測定方法について説明する。
図1は本発明による水中アンモニア測定方法を採用する
ときのバッチ連続式水中アンモニア測定装置の系統図で
ある。図1においてバッチ連続式水中アンモニア測定装
置1は主要部として試料水を気相部3を形成して一定量
保持し、攪拌子4を有する攪拌器5を備える測定セル6
と、測定セル6の気相部3に移行したアンモニアガスを
検知する隔膜式のアンモニアガス電極7と、採水ポンプ
8及びピンチ弁9を介して測定セル6に注入する試料水
を採取する採水槽10と、測定セル6内の試料水にアル
カリポンプ11を介して注入するアルカリを貯留するア
ルカリタンク12と、測定セル6にピンチ弁13,14
及び採水ポンプ8を介して供給する既知の異なるアンモ
ニア濃度の標準溶液を貯留するゼロ液タンク16及びス
パン液タンク17と、試料水を測定セル6からオーバフ
ローさせるピンチ弁18及び排液させるピンチ弁19
と、測定セル6に空気を流入させる電磁弁20と、測定
セル6内の試料水の温度を所定の一定温度に保持するヒ
ータ22及び温調器23と、アンモニアガス電極7の出
力から試料水中のアンモニア濃度を算出し、又各種ピン
チ弁,ポンプ等をあらかじめ記憶されたシーケンスプロ
グラムに従って制御する演算制御器25とから構成され
る。なお24は初段アンプである。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS A batch continuous method for measuring ammonia in water according to an embodiment of the present invention will be described below with reference to the drawings.
FIG. 1 is a system diagram of a batch continuous type aqueous ammonia measuring device when the method for measuring aqueous ammonia according to the present invention is adopted. In FIG. 1, a batch continuous type ammonia measuring device 1 has a measuring cell 6 as a main part, which forms a gas phase part 3 and holds a fixed amount of sample water, and includes a stirrer 5 having a stirrer 4.
A diaphragm type ammonia gas electrode 7 for detecting the ammonia gas transferred to the gas phase part 3 of the measurement cell 6, and a sample water to be injected into the measurement cell 6 via a water sampling pump 8 and a pinch valve 9. A water tank 10, an alkali tank 12 for storing alkali to be injected into the sample water in the measurement cell 6 via an alkali pump 11, and pinch valves 13, 14 in the measurement cell 6.
And a zero liquid tank 16 and a span liquid tank 17 for storing standard solutions of known different ammonia concentrations supplied via the water sampling pump 8, a pinch valve 18 for overflowing the sample water from the measurement cell 6, and a pinch valve for draining the sample water. 19
A solenoid valve 20 for introducing air into the measurement cell 6, a heater 22 and a temperature controller 23 for maintaining the temperature of the sample water in the measurement cell 6 at a predetermined constant temperature, and an output of the ammonia gas electrode 7 And an arithmetic controller 25 for controlling various pinch valves, pumps and the like according to a sequence program stored in advance. Reference numeral 24 is a first stage amplifier.
【0012】ここで、測定セル6及びアンモニアガス電
極7は外気温の影響を除くために恒温槽26の中に収納
されている。このような構成により試料水中のアンモニ
ア濃度を測定する手順は次記のようにして行なわれる。
採水槽10から採水ポンプ8により測定セル6に試料水
が注入される。このとき、ピンチ弁9,18,19は
開、ピンチ弁13,14は閉である。この状態で測定セ
ル6に注入した試料水はピンチ弁18を介してオーバフ
ローし、一方ピンチ弁19を介して排液して測定セル6
の内部を洗浄する。洗浄終了後、ピンチ弁19を閉に
し、測定セル6内の試料水をオーバフローさせて一定量
にした後ピンチ弁9,18を閉にして採水ポンプ8を停
止する。そしてアルカリポンプ11を駆動してアルカリ
タンク12からアルカリを測定セル6内に注入し、試料
水をpH11以上にする。そして同時にヒータ22によ
り試料水を加熱し、温調器23により一定温度に保持
し、攪拌器5の攪拌子4により攪拌し、試料水中の溶存
アンモニアをガス化して気相部3に移行させる。Here, the measuring cell 6 and the ammonia gas electrode 7 are housed in a constant temperature bath 26 in order to eliminate the influence of the outside temperature. The procedure for measuring the ammonia concentration in the sample water with such a configuration is performed as follows.
Sample water is injected from the water sampling tank 10 into the measurement cell 6 by the water sampling pump 8. At this time, the pinch valves 9, 18, 19 are open, and the pinch valves 13, 14 are closed. In this state, the sample water injected into the measurement cell 6 overflows via the pinch valve 18 and is drained via the pinch valve 19 to be discharged to the measurement cell 6
Wash the inside of the. After the cleaning is completed, the pinch valve 19 is closed, the sample water in the measuring cell 6 is overflowed to a fixed amount, and then the pinch valves 9 and 18 are closed to stop the water sampling pump 8. Then, the alkali pump 11 is driven to inject the alkali from the alkali tank 12 into the measurement cell 6, and the sample water is adjusted to pH 11 or higher. At the same time, the sample water is heated by the heater 22, kept at a constant temperature by the temperature controller 23, stirred by the stirrer 4 of the stirrer 5, and the dissolved ammonia in the sample water is gasified and transferred to the gas phase part 3.
【0013】アンモニアガス電極7は気相部3に移行し
たアンモニアガスを検知し、これにより生じる電極出力
に基づいてあらかじめ作製した検量線に従って演算制御
器25により試料水のアンモニア濃度を定量する。この
ようなアンモニア濃度の測定はバッチ式に連続して行な
われ、検量線は定期的に下記の手順により求められる。The ammonia gas electrode 7 detects the ammonia gas transferred to the gas phase portion 3, and the arithmetic controller 25 quantifies the ammonia concentration of the sample water according to a calibration curve prepared in advance based on the electrode output generated by the ammonia gas. Such measurement of the ammonia concentration is continuously performed in a batch system, and a calibration curve is periodically obtained by the following procedure.
【0014】前述のように測定セル6等の内部を洗浄し
て測定セル6の内部を空にした後、ピンチ弁13を開に
して採水ポンプ8によりゼロ液タンク16から既知のア
ンモニア濃度のゼロ液を測定セル6内に注入し、オーバ
フローさせて一定量保持する。そして前述と同様にアル
カリタンク12からアルカリを加えてpH11以上に
し、ヒータ22により加熱して一定温度にし、攪拌器5
の攪拌子4で攪拌し、安定したところでアンモニアガス
電極7で検知して得られた電極出力を演算制御器25に
記憶させる。After cleaning the inside of the measuring cell 6 and the like to empty the inside of the measuring cell 6 as described above, the pinch valve 13 is opened and the sampling pump 8 is used to remove a known ammonia concentration from the zero liquid tank 16. Zero solution is injected into the measuring cell 6 and allowed to overflow to maintain a constant amount. Then, in the same manner as described above, the alkali is added from the alkali tank 12 to adjust the pH to 11 or more, and the heater 22 is used to heat the mixture to a constant temperature.
After stirring with the stirrer 4, the electrode output obtained by detecting with the ammonia gas electrode 7 when stable is stored in the arithmetic controller 25.
【0015】上記の操作終了後測定セル6のゼロ液をピ
ンチ弁19を開にして排液し、前述のように洗浄した後
測定セル6の内部を空にする。そしてスパン液タンク1
7からゼロ液のアンモニア濃度と異なる濃度のアンモニ
アを有するサンプ液をゼロ液の場合と同じ手順により測
定セル6に注入し、加熱,攪拌して気相部3に移行した
アンモニアガスをアンモニアガス電極7により検知し、
得られた電極出力を演算制御器25に記憶させる。そし
て演算制御器25にてゼロ液とサンプ液との異なるアン
モニア濃度に対応して検知して得られたアンモニアガス
電極の異なる出力から検量線が作製される。After the above operation is completed, the zero liquid in the measuring cell 6 is drained by opening the pinch valve 19 and washed as described above, and then the inside of the measuring cell 6 is emptied. And span liquid tank 1
The sump liquid containing ammonia having a concentration different from that of the zero liquid from 7 is injected into the measurement cell 6 by the same procedure as in the case of the zero liquid, and the ammonia gas transferred to the gas phase part 3 by heating and stirring is added to the ammonia gas electrode. Detected by 7,
The obtained electrode output is stored in the arithmetic controller 25. Then, a calibration curve is created from the different outputs of the ammonia gas electrodes obtained by detecting the different ammonia concentrations of the zero liquid and the sump liquid by the arithmetic controller 25.
【0016】ここで、ゼロ液とサンプ液のアンモニア濃
度はそれぞれ測定装置の測定レンジの下限,上限近くの
濃度であることが望ましい。なお、電磁弁20は測定セ
ル6内の試料水等を排出するときピンチ弁19とともに
開にされる。ここで、前記測定セル6内の洗浄後試料水
を注入してアンモニアガス電極7でアンモニアガス濃度
を検知し、定期的に検量線を作製してバッチ連続式に水
中のアンモニア濃度を測定するためのピンチ弁9,1
3,14,18,19,電磁弁20の開閉,採水ポンプ
8,アルカリポンプ11の起動,停止は演算制御器25
に記憶されたシーケンスプログラムに従って行なわれ
る。Here, it is desirable that the ammonia concentrations of the zero liquid and the sump liquid are near the lower and upper limits of the measuring range of the measuring device, respectively. The electromagnetic valve 20 is opened together with the pinch valve 19 when the sample water or the like in the measuring cell 6 is discharged. Here, in order to measure the ammonia concentration in water in a batch continuous manner by injecting sample water after cleaning in the measurement cell 6 and detecting the ammonia gas concentration at the ammonia gas electrode 7 and periodically creating a calibration curve. Pinch valve 9,1
3, 14, 18, 19, the opening and closing of the solenoid valve 20, the start and stop of the water sampling pump 8, the alkaline pump 11 are the arithmetic and control unit 25.
Is performed according to the sequence program stored in.
【0017】[0017]
【発明の効果】以上の説明から明らかなように、本発明
によれば前述の水中のアンモニア濃度の測定方法によ
り、バッチ式のため、試料水をpH11以上にするため
に常時アルカリを注入することなく、また標準溶液を混
入しないことから薬品使用量や排液量が減少する。また
従来のように標準溶液の混入でなく、検量線の作製によ
りアンモニア濃度を定量するので、標準溶液の注入精度
が要求されない。さらにバッチ式のためアンモニアガス
電極の出力の安定化が早くなり、全体の応答も短かくな
り、また薬品の使用量の減少や配管のスケール等による
汚れが少なくなるので、メンテナンスが容易で長期にわ
たり安定した水中のアンモニア濃度の測定が可能とな
る。As is apparent from the above description, according to the present invention, the method for measuring the ammonia concentration in water described above is a batch method, so that alkali is constantly injected to make the pH of the sample water 11 or more. Also, since no standard solution is mixed, the amount of chemicals used and the amount of drainage are reduced. Further, since the ammonia concentration is quantified by preparing a calibration curve instead of mixing the standard solution as in the conventional case, the injection accuracy of the standard solution is not required. In addition, the batch type output stabilizes the output of the ammonia gas electrode quickly, shortens the overall response, reduces the amount of chemicals used, and reduces fouling due to pipe scales, etc. It is possible to stably measure the ammonia concentration in water.
【図1】本発明の実施例による水中アンモニアの測定方
法を採用するときのバッチ連続式水中アンモニア測定装
置の系統図FIG. 1 is a system diagram of a batch continuous type aqueous ammonia measuring device when the method for measuring aqueous ammonia according to an embodiment of the present invention is adopted.
1 バッチ連続式水中アンモニア測定装置 3 気相部 4 攪拌子 5 攪拌器 6 測定セル 7 アンモニアガス電極 10 採水槽 12 アルカリタンク 16 ゼロ液タンク 17 スパン液タンク 22 ヒータ 23 温調器 25 演算制御器 26 恒温槽 1 Batch Continuous Type Ammonia Measuring Device 3 Gas Phase Section 4 Stirrer 5 Stirrer 6 Measuring Cell 7 Ammonia Gas Electrode 10 Water Collection Tank 12 Alkaline Tank 16 Zero Liquid Tank 17 Span Liquid Tank 22 Heater 23 Temperature Controller 25 Calculation Controller 26 Constant temperature bath
Claims (1)
形成して一定量の試料水を注水し、同時にアルカリを加
えてpH11以上にした後、試料水を一定温度に保持し
て攪拌し、試料水中のアンモニアをガス化して気相部に
移行させ、この気相部のアンモニアガスを隔膜式アンモ
ニアガス電極で検知して得られる出力からあらかじめ作
製する検量線に基づいて試料水中のアンモニア濃度を定
量することを特徴とするバッチ連続式水中アンモニア測
定方法。1. A vapor phase part is formed in a measuring cell housed in a constant temperature bath to inject a fixed amount of sample water, and at the same time, alkali is added to adjust the pH to 11 or more, and then the sample water is kept at a constant temperature. Agitation to gasify the ammonia in the sample water, transfer it to the gas phase, and detect the ammonia gas in the gas phase with the diaphragm type ammonia gas electrode. A batch continuous method for measuring ammonia in water, which comprises quantifying the ammonia concentration in water.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP4177255A JPH0618474A (en) | 1992-07-06 | 1992-07-06 | Batch continuous method for measuring ammonia in water |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP4177255A JPH0618474A (en) | 1992-07-06 | 1992-07-06 | Batch continuous method for measuring ammonia in water |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH0618474A true JPH0618474A (en) | 1994-01-25 |
Family
ID=16027881
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP4177255A Pending JPH0618474A (en) | 1992-07-06 | 1992-07-06 | Batch continuous method for measuring ammonia in water |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0618474A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4895353A (en) * | 1988-06-28 | 1990-01-23 | The Pullman Company | Fluid filled elastomeric damping device |
| CN109827917A (en) * | 2019-03-28 | 2019-05-31 | 中国三峡建设管理有限公司 | Ammonia burst size CONTINUOUS VISCOSITY MEASURING and method in a kind of concrete |
| CN117030827A (en) * | 2023-08-23 | 2023-11-10 | 上海仪电科学仪器股份有限公司 | System for detecting ammonia nitrogen based on electrode method |
-
1992
- 1992-07-06 JP JP4177255A patent/JPH0618474A/en active Pending
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4895353A (en) * | 1988-06-28 | 1990-01-23 | The Pullman Company | Fluid filled elastomeric damping device |
| CN109827917A (en) * | 2019-03-28 | 2019-05-31 | 中国三峡建设管理有限公司 | Ammonia burst size CONTINUOUS VISCOSITY MEASURING and method in a kind of concrete |
| CN117030827A (en) * | 2023-08-23 | 2023-11-10 | 上海仪电科学仪器股份有限公司 | System for detecting ammonia nitrogen based on electrode method |
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