JPH095315A - Method and device for analyzing concentrated solution - Google Patents
Method and device for analyzing concentrated solutionInfo
- Publication number
- JPH095315A JPH095315A JP7159071A JP15907195A JPH095315A JP H095315 A JPH095315 A JP H095315A JP 7159071 A JP7159071 A JP 7159071A JP 15907195 A JP15907195 A JP 15907195A JP H095315 A JPH095315 A JP H095315A
- Authority
- JP
- Japan
- Prior art keywords
- solution
- halogen
- concentration
- corrosion rate
- metal
- 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)
- Investigating And Analyzing Materials By Characteristic Methods (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、金属製容器内で濃縮さ
れたハロゲン溶液中のハロゲン濃度を分析するのに最適
な濃厚溶液の分析方法に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a concentrated solution analysis method most suitable for analyzing the halogen concentration in a halogen solution concentrated in a metal container.
【0002】[0002]
【従来の技術】ごみ焼却プラント及び化学プラントが取
り扱う流体中には腐食性の強い塩素(Cl2)、臭素
(Br2)及びヨウ素(I2)等のハロゲンガスが含まれ
ており、これらのハロゲンガスが溶液を保有する容器を
流通すると、容器内の溶液は気相中のハロゲン分子と接
触することにより、ヘンリー則に従う平衡濃度までハロ
ゲン分子を気相中より吸収する。しかし、容器が金属製
であると腐食性のハロゲンガスにより金属が腐食され、
それと共に溶液中のハロゲン元素濃度がヘンリー則に従
う平衡濃度の数十倍も濃縮されて濃度が高くなり、溶液
中や高湿度部分においては腐食による装置のリーク事故
が発生する要因となっている。このため、ごみ焼却プラ
ントでは腐食が濃度に影響されるので運転期間中に濃縮
したハロゲン濃度を分析して、腐食に対する対策を講じ
る必要性がでてくる。従来は濃縮されたハロゲンの濃度
測定はプラントよりサンプル液を採取し、外部の分析ラ
ボまで持ち帰り分析していた。溶液中のハロゲン分子あ
るいはイオン濃度の定量的分析は滴定法や光分析法が用
いられている。滴定法ではサンプリングした液に他の試
薬を添加して定量する。ヘンリー則に従う平衡濃度に達
した溶液濃度が薄いハロゲン分子の濃度は通常吸光光度
法を用いて原液の状態で分析できる。吸光光度法は溶液
に光を照射し、溶液に吸収された光量により濃度を求め
るもので金属の腐食を引き起すような濃厚溶液の分析は
困難である。ヨウ素イオン(I3~)では約3×10~4mo
l/lが直接分析の限界である。2. Description of the Related Art Fluids handled by refuse incineration plants and chemical plants contain halogen gases such as highly corrosive chlorine (Cl 2 ), bromine (Br 2 ) and iodine (I 2 ). When the halogen gas flows through the container holding the solution, the solution in the container comes into contact with the halogen molecules in the gas phase to absorb the halogen molecules from the gas phase to an equilibrium concentration according to Henry's law. However, if the container is made of metal, corrosive halogen gas corrodes the metal,
At the same time, the concentration of the halogen element in the solution is concentrated by several tens of times the equilibrium concentration according to Henry's law, and the concentration becomes high, which causes a leak accident of the device due to corrosion in the solution or in the high humidity portion. For this reason, in a refuse incineration plant, since corrosion is affected by the concentration, it is necessary to analyze the halogen concentration concentrated during the operation period and take countermeasures against the corrosion. Conventionally, the concentration of concentrated halogen was measured by taking a sample solution from the plant and bringing it back to an external analytical laboratory for analysis. A titration method or an optical analysis method is used for quantitative analysis of the halogen molecule or ion concentration in the solution. In the titration method, other reagents are added to the sampled solution for quantification. The concentration of a halogen molecule whose solution concentration has reached an equilibrium concentration according to the Henry's law can usually be analyzed in the state of a stock solution by using an absorptiometric method. The absorptiometric method irradiates a solution with light and determines the concentration based on the amount of light absorbed in the solution, and it is difficult to analyze a concentrated solution that causes metal corrosion. About 3 × 10 ~ 4 mo with iodine ion (I 3 ~)
l / l is the limit of direct analysis.
【0003】[0003]
【発明が解決しようとする課題】上記の従来の吸光光度
法による分析方法ではサンプリングした高濃度のハロゲ
ン溶液をそのまま分析することは困難であり、希釈する
と溶液の緩衝作用の影響を受けやすくなる。また、プラ
ントよりサンプリングし外部の分析ラボに搬送するバッ
チ分析のため、濃度が判明するまで時間がかかる。本発
明の目的は、金属容器と接触しているハロゲン濃厚溶液
をリアルタイムで分析することにある。However, it is difficult to analyze the sampled high-concentration halogen solution as it is by the above-mentioned conventional absorptiometric analysis method, and when it is diluted, it is easily affected by the buffer action of the solution. In addition, since it is a batch analysis in which it is sampled from the plant and transported to an external analysis lab, it takes time to determine the concentration. It is an object of the present invention to analyze a concentrated halogen solution in contact with a metal container in real time.
【0004】[0004]
【課題を解決するための手段】上記目的は、濃縮された
ハロゲン溶液を保有する金属容器の腐食速度を測定し、
金属腐食速度の測定値を用いて電気化学的な手法により
ハロゲン濃度を求めることにより達成される。The above object is to measure the corrosion rate of a metal container containing a concentrated halogen solution,
This is achieved by determining the halogen concentration by an electrochemical method using the measured value of the metal corrosion rate.
【0005】[0005]
【作用】Cl2,Br2及びI2のようなハロゲンが供給
される溶液や湿潤な気相中に形成された液滴内のハロゲ
ン分子は錯イオン、例えばCl3~,Br3~及びI3~の形
でそれらが接する金属を腐食させ、時間と共に濃縮して
行く。今、溶液(あるいは液滴)の体積をV、溶液と接
する金属の面積をS、ハロゲン分子とその錯イオン間の
平衡定数をK、金属の原子量をWm、ハロゲン分子濃度
をCh2、その錯イオン濃度をCh3~及び金属の腐食速
度をmとする時、錯イオン濃度Ch3~は次式で与えられ
る。Halogen molecules in droplets formed in a solution to which halogens such as Cl 2 , Br 2 and I 2 are supplied or in a wet gas phase are complex ions such as Cl 3 ~, Br 3 ~ and I. Corrodes the metals they come into contact with in the form of 3 ~, and concentrates over time. Now, the volume of the solution (or droplet) is V, the area of the metal in contact with the solution is S, the equilibrium constant between the halogen molecule and its complex ion is K, the atomic weight of the metal is Wm, the halogen molecule concentration is Ch 2 , and the complex When the ion concentration is Ch 3 ~ and the metal corrosion rate is m, the complex ion concentration Ch 3 ~ is given by the following equation.
【0006】[0006]
【数2】 [Equation 2]
【0007】溶液中のハロゲン分子濃度Ch2は系に供
給されるハロゲンガス濃度が与えられるとヘンリー則に
より決定される。平衡定数KはCl2(Cl~+Cl2⇔
Cl3~)に対してK≒0.2,Br2(Br~+Br2⇔B
r3~)に対しては23.6及びI2(I~+I2⇔I3~)に
対しては710(共に室温)である。従って、(1)式
より金属の腐食速度mを電気化学的センサを用いてリア
ルタイムで測定することにより液中のハロゲン分子濃度
をハロゲン錯イオン濃度としてその場で測定することが
可能となる。液が多量の溶液でなく、水滴のような微量
な液でも液内に濃縮した濃厚なハロゲン元素濃度は
(1)式を用いて原液の状態で分析できる。金属の種類
あるいは腐食性ガスの濃度の大きさによっては金属の表
面の腐食形態は全面腐食、孔食あるいは粒界腐食と異っ
てくるが腐食速度mの値はこれら金属の腐食形態には依
存しないで溶解電流に依存する。従って金属の腐食速度
mは直流的に分極抵抗を測定したり、交流インピーダン
スを測定する電気化学的センサによって経時的にリアル
タイムで測定可能である。The halogen molecule concentration Ch 2 in the solution is determined by the Henry's law given the concentration of the halogen gas supplied to the system. The equilibrium constant K is Cl 2 (Cl ~ + Cl 2 ⇔
For Cl 3 ~), K≈0.2, Br 2 (Br ~ + Br 2 ⇔ B
It is 23.6 for r 3 ~) and 710 for I 2 (I ~ + I 2 ⇔ I 3 ~) (both at room temperature). Therefore, by measuring the corrosion rate m of the metal in real time from the equation (1) using an electrochemical sensor, it becomes possible to measure the halogen molecule concentration in the liquid as the halogen complex ion concentration in situ. Even if a liquid is not a large amount of liquid but a small amount of liquid such as water droplets, the concentrated concentration of halogen element in the liquid can be analyzed in the state of undiluted liquid by using the formula (1). Depending on the type of metal or the concentration of corrosive gas, the corrosion form of the metal surface differs from general corrosion, pitting corrosion or intergranular corrosion, but the value of the corrosion rate m depends on the corrosion form of these metals. Do not depend on the melting current. Therefore, the corrosion rate m of the metal can be measured in real time over time by measuring the polarization resistance in a direct current or by an electrochemical sensor measuring an alternating current impedance.
【0008】[0008]
【実施例】以下、本発明の実施例を図により詳細に説明
する。図1は本発明の実施例の構成を示すブロック図で
ある。本図に示すように1は金属製容器、2はハロゲン
溶液、3は腐食速度モニタリングセンサ、4は温度セン
サ、5はハロゲンを含むガス、6は図示せざるキイボー
ドを含む入力部、7はマイコンによる演算部、8はCR
Tによる表示部、9はプリンタによる記録部9である。
金属製容器1に外部よりハロゲンを含むガス5が供給さ
れる。金属製容器1内のハロゲン溶液2の内部には金属
製容器1の腐食速度をモニタする腐食速度モニタリング
センサ3及び温度センサ4が設置されている。これらの
センサ3,4は入力部6に接続され、演算部7で溶液内
ハロゲン濃度が分析される。これらのデータは表示部8
で表示され、さらに記録部9で記録される。Embodiments of the present invention will now be described in detail with reference to the drawings. FIG. 1 is a block diagram showing the configuration of an embodiment of the present invention. As shown in the figure, 1 is a metal container, 2 is a halogen solution, 3 is a corrosion rate monitoring sensor, 4 is a temperature sensor, 5 is a gas containing halogen, 6 is an input unit including a key board (not shown), and 7 is a microcomputer. Computation part by, 8 is CR
A display unit 9 by T, and a recording unit 9 by a printer.
A gas 5 containing halogen is supplied to the metal container 1 from the outside. A corrosion rate monitoring sensor 3 and a temperature sensor 4 for monitoring the corrosion rate of the metal container 1 are installed inside the halogen solution 2 in the metal container 1. These sensors 3 and 4 are connected to the input unit 6, and the computing unit 7 analyzes the halogen concentration in the solution. These data are displayed on the display unit 8.
Is displayed and is recorded by the recording unit 9.
【0009】図2は本発明の実施例の動作を示すフロー
チャートである。本図は濃厚なハロゲン濃度をリアルタ
イムで分析する工程を示している。初にステップ10で
入力部6の図示せざるキイボードからハロゲン溶液2の
体積Vがインプットされ、同様にステップ11でハロゲ
ン溶液2と接する金属製容器1の面積Sがインプットさ
れる。さらにステップ12で金属の原子量Wmがインプ
ットされる。平衡定数Kは温度に依存する定数であり、
ステップ13で測定されたハロゲン溶液2の温度におけ
る平衡定数Kがステップ14でインプットされる。ステ
ップ15でインプットされた金属製容器1の気相中のハ
ロゲン分子濃度を用いて、ステップ16でハロゲン溶液
2中のハロゲン分子濃度Ch2がステップ13で測定さ
れたハロゲン溶液2の温度を用いて演算される。ステッ
プ17で金属製容器1を構成する金属の腐食速度mが計
測され、ステップ18で(1)式を用いてハロゲン元素
濃度が算出される。ステップ19で算出したハロゲン元
素濃度がCRTに表示され、ステップ20でプリンタか
ら打出される。FIG. 2 is a flow chart showing the operation of the embodiment of the present invention. This figure shows the step of analyzing the rich halogen concentration in real time. First, in step 10, the volume V of the halogen solution 2 is input from a key board (not shown) of the input unit 6, and similarly, in step 11, the area S of the metal container 1 in contact with the halogen solution 2 is input. Further, in step 12, the atomic weight Wm of the metal is input. The equilibrium constant K is a constant that depends on temperature,
The equilibrium constant K at the temperature of the halogen solution 2 measured in step 13 is input in step 14. Using the halogen molecule concentration in the gas phase of the metal container 1 input in step 15, the halogen molecule concentration Ch 2 in the halogen solution 2 in step 16 is calculated using the temperature of the halogen solution 2 measured in step 13. Is calculated. In step 17, the corrosion rate m of the metal forming the metal container 1 is measured, and in step 18, the halogen element concentration is calculated using the equation (1). The halogen element concentration calculated in step 19 is displayed on the CRT, and is ejected from the printer in step 20.
【0010】以上述べたように本実施例によれば、ハロ
ゲンガスを供給された溶液あるいは液滴内に濃縮したハ
ロゲン元素濃度は金属製容器の腐食速度が電気化学的方
法により測定可能なのでリアルタイムで原液の状態で分
析可能である。さらに地球温暖化防止のためのCO2吸
収装置の吸収液も時間と共に濃縮すると同時に金属を腐
食させるので、本実施例により濃厚溶液を原液の状態で
分析することが可能である。As described above, according to this embodiment, the concentration of the halogen element concentrated in the solution or the liquid droplets to which the halogen gas is supplied can be measured in real time because the corrosion rate of the metal container can be measured by an electrochemical method. It can be analyzed as a stock solution. Further, since the absorption liquid of the CO 2 absorption device for the prevention of global warming also concentrates with time and corrodes the metal, it is possible to analyze the concentrated solution in the state of undiluted solution according to the present embodiment.
【0011】[0011]
【発明の効果】本発明によれば、金属の腐食速度を電気
化学的センサを用いてリアルタイムで測定し、演算によ
り溶液中のハロゲン分子濃度をその場で分析することが
可能となる。According to the present invention, the corrosion rate of metal can be measured in real time using an electrochemical sensor, and the halogen molecule concentration in the solution can be analyzed in situ by calculation.
【図1】本発明の実施例の構成を示すブロック図であ
る。FIG. 1 is a block diagram showing a configuration of an exemplary embodiment of the present invention.
【図2】本発明の実施例の動作を示すフローチャートで
ある。FIG. 2 is a flowchart showing the operation of the embodiment of the present invention.
1 金属製容器 2 ハロゲン溶液 3 腐食速度モニタリングセンサ 4 温度センサ 5 ハロゲンを含むガス 6 入力部 7 演算部 8 表示部 9 記録部 1 Metal Container 2 Halogen Solution 3 Corrosion Rate Monitoring Sensor 4 Temperature Sensor 5 Gas Containing Halogen 6 Input Section 7 Computing Section 8 Display Section 9 Recording Section
Claims (3)
容器の腐食速度を測定し、該金属腐食速度の測定値と、
前記ハロゲン溶液と前記金属容器の接触面積と、前記金
属容器の金属原子量と、前記ハロゲン溶液の体積と、ハ
ロゲン分子とその錯イオン間の平衡定数と、該ハロゲン
分子濃度とを用いて関係式により前記ハロゲン溶液のハ
ロゲン錯イオン濃度を求めることを特徴とする濃厚溶液
の分析方法。1. A corrosion rate of a metal container holding a concentrated halogen solution is measured, and a measured value of the metal corrosion rate is included.
The contact area between the halogen solution and the metal container, the amount of metal atoms in the metal container, the volume of the halogen solution, the equilibrium constant between the halogen molecule and its complex ion, and the concentration of the halogen molecule are used according to a relational expression. A method for analyzing a concentrated solution, which comprises determining a halogen complex ion concentration of the halogen solution.
度を下記の式により求めることを特徴とする請求項1に
記載の濃厚溶液の分析方法。 【数1】 2. The method for analyzing a concentrated solution according to claim 1, wherein the halogen complex ion concentration of the halogen solution is determined by the following formula. [Equation 1]
金属容器の腐食速度を測定する手段と、該金属腐食速度
の測定値を入力して前記ハロゲン溶液のハロゲン濃度を
演算する手段とを有することを特徴とする濃厚溶液の分
析装置。3. A unit for measuring a corrosion rate of a metal container holding a concentrated halogen solution, and a unit for inputting a measured value of the metal corrosion rate to calculate a halogen concentration of the halogen solution. A concentrated solution analyzer characterized by the following.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP7159071A JPH095315A (en) | 1995-06-26 | 1995-06-26 | Method and device for analyzing concentrated solution |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP7159071A JPH095315A (en) | 1995-06-26 | 1995-06-26 | Method and device for analyzing concentrated solution |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH095315A true JPH095315A (en) | 1997-01-10 |
Family
ID=15685589
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP7159071A Pending JPH095315A (en) | 1995-06-26 | 1995-06-26 | Method and device for analyzing concentrated solution |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH095315A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR100888739B1 (en) * | 2007-06-08 | 2009-03-17 | 한국에너지기술연구원 | The device and method on absorption equilibrium test of absorbent for remove of carbon dioxide from flue gas |
-
1995
- 1995-06-26 JP JP7159071A patent/JPH095315A/en active Pending
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR100888739B1 (en) * | 2007-06-08 | 2009-03-17 | 한국에너지기술연구원 | The device and method on absorption equilibrium test of absorbent for remove of carbon dioxide from flue gas |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| Environmental Monitoring Systems Laboratory (Cincinnati | Methods for the determination of inorganic substances in environmental samples | |
| US4757707A (en) | Molten metal gas analysis | |
| US5269832A (en) | Method and apparatus for continuously measuring the concentration of chemicals in solutions | |
| IT1306112B1 (en) | METHOD FOR THE QUANTITATIVE ANALYSIS OF THE ATOMIC COMPONENTS OF MATERIALS BY MEANS OF LIBS SPECTROSCOPY MEASURES WITHOUT CALIBRATION | |
| Marshall et al. | An introduction to open-path FT-IR atmospheric monitoring | |
| Przybylko et al. | The determination of aqueous ammonia by ion mobility spectrometry | |
| Fontela et al. | Carbonate system species and pH | |
| Hinds et al. | Measurement of pH in concentrated brines | |
| Stocking et al. | An automated technique for the simultaneous determination of cations in nanoliter volumes | |
| Smith | Intra-workday fluctuations of airborne contaminant concentration and the time-weighted average | |
| JP3018726B2 (en) | Acid rain automatic measuring device | |
| US4165630A (en) | Continuous in-stack pollutant monitoring system | |
| JP5855981B2 (en) | Mercury analyzer and mercury analysis system | |
| JP2003028852A (en) | Analyzer for element in sample | |
| Espinoza-Nava et al. | Sampling and Analysis Methodology Review to Report Total PFC Emissions | |
| Stockwell et al. | Monitoring elemental mercury in an urban environment | |
| Spěváčková et al. | Sampling procedure and a radio-indicator study of mercury determination in whole blood by using an AMA 254 atomic absorption spectrometer | |
| JPH10239289A (en) | Inline acid concentration measurement method and measurement probe | |
| Pissenberger et al. | Automatic cleanness determination of production samples with OES/PDA | |
| Sauren et al. | On the adsorption properties of ammonia to various surfaces | |
| Quevauviller | Traceability of environmental chemical analyses: can theory match practice? | |
| Zhao et al. | Interference in Analysis of Hydrogen Chloride by Ion Chromatography and Quality Control Measures | |
| JPH067306Y2 (en) | Analysis equipment | |
| Smith | Methods for the determination of hydrogen distribution in high strength steel | |
| JPH07209173A (en) | Method and apparatus for estimating statistical and probabilistic quantity of corrosion |