JPS63173962A - Wet acid type total organic carbon measuring method and apparatus - Google Patents

Wet acid type total organic carbon measuring method and apparatus

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Publication number
JPS63173962A
JPS63173962A JP62006971A JP697187A JPS63173962A JP S63173962 A JPS63173962 A JP S63173962A JP 62006971 A JP62006971 A JP 62006971A JP 697187 A JP697187 A JP 697187A JP S63173962 A JPS63173962 A JP S63173962A
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JP
Japan
Prior art keywords
solution
sample
carrier gas
organic carbon
tank
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
JP62006971A
Other languages
Japanese (ja)
Inventor
Yozo Morita
洋造 森田
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.)
Shimadzu Corp
Original Assignee
Shimadzu Corp
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Filing date
Publication date
Application filed by Shimadzu Corp filed Critical Shimadzu Corp
Priority to JP62006971A priority Critical patent/JPS63173962A/en
Publication of JPS63173962A publication Critical patent/JPS63173962A/en
Pending legal-status Critical Current

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  • Investigating Or Analyzing Non-Biological Materials By The Use Of Chemical Means (AREA)
  • Investigating Or Analysing Materials By The Use Of Chemical Reactions (AREA)
  • Investigating Or Analysing Materials By Optical Means (AREA)

Abstract

PURPOSE:To dispense with the measurement and correction of a blank value, by heating an oxidation agent acid solution to remove total carbon components contained in the solution through the conversion thereof into CO2. CONSTITUTION:A fixed amount of an oxidation agent solution and an acid solution are sent to an aeration tank 37 from an oxidation solution tank 30 and from an acid solution tank 31. The solution is heated with a heating furnace 38 and total carbon in the solution is converted into CO2. Then, a carrier gas is sent to the aeration tank 37 from a carrier gas supply section to remove CO2. Thereafter, the solution is transferred to a reaction tank 40 and a fixed amount of a sample is injected from a microsyringe 41. After heating with the heating furnace 42, a valve 22 is opened to introduce the carrier gas and CO2 generated is sent via a water separator 45 and a dehumidifier 46 to a CO2 detector 48. This reduces the total carbon contained in the oxidation agent acid solution to a small level, thereby eliminating the need for operations of measuring and correcting blank values with a smaller blank value due to the oxidation agent and acid.

Description

【発明の詳細な説明】 イ)超楽上の利用分骨 この発明は、無機RJArA分(I <: )を含有せ
ず有機炭素成分(OC)を含有する水性系試料の湿式波
化式全有機憔炭素(’roe>測定法および裟はの改良
に関する。
DETAILED DESCRIPTION OF THE INVENTION A) Ultra-easy Utilization Features This invention is a complete wet wave treatment method for aqueous samples containing organic carbon components (OC) but not inorganic RJArA components (I<:). This paper relates to a method for measuring organic carbon dioxide ('roe) and improvements to the body.

(ロ)従来の技術と問題点 OC含有の水性系試料の湿式酸化式TOO測定法として
は、ペルオキソ硫酸カリウムなどの酸化剤の酸性溶液ま
たはこれに紫外線を併用して試料に作用させて、そのO
C成分を二酸化炭素(002)に変換し、これを測定す
る方法が行われている。
(b) Conventional techniques and problems The wet oxidation TOO measurement method for aqueous samples containing OC involves using an acidic solution of an oxidizing agent such as potassium peroxosulfate or a combination of ultraviolet rays to act on the sample. O
A method is being used in which the C component is converted into carbon dioxide (002) and then measured.

第1図は、従来用いられている湿式酸化式TOO測定装
置の構成説明図であるが次のように操作されている。
FIG. 1 is an explanatory diagram of the configuration of a conventionally used wet oxidation TOO measuring device, which is operated as follows.

a、一定量のOC含有試料を、マイクロシリンジ7によ
り試料注入口6を通じて反応槽4に入れる。
a. A certain amount of OC-containing sample is introduced into the reaction tank 4 through the sample injection port 6 using the microsyringe 7.

b、一定量の酸化剤(例えばペルオキソ硫酸カリウム)
の水溶液と一定量の酸(例えばリン酸)の水溶液とをそ
れぞれ、酸化剤溶液槽8と酸溶液槽9とから定量ポンプ
10と11によって導管12と18を通じて反応槽4に
注入する。
b. a certain amount of oxidizing agent (e.g. potassium peroxosulfate);
and a certain amount of an aqueous solution of an acid (for example, phosphoric acid) are injected from the oxidizer solution tank 8 and the acid solution tank 9 into the reaction tank 4 through the conduits 12 and 18 by metering pumps 10 and 11, respectively.

C1反応槽4を加熱炉6によって、試料中の00成分を
CO2に変換するのに充分な温度と時間で加熱した後、
次にキャリアガスガス供給部1のバルブ2を開いて管路
8を通じて一定流量のキャリアガスを流し、反応槽4内
の試料と酸化剤および酸との見合夜中を通過させて、前
記OC成分由来の002 をキャリアガスによって水分
離器14と除湿器15を通過させて水分と湿分を除去し
次いでCO2検出器17に送りCO2を検出する。
After heating the C1 reaction tank 4 with the heating furnace 6 at a temperature and time sufficient to convert the 00 component in the sample into CO2,
Next, the valve 2 of the carrier gas gas supply unit 1 is opened to allow a constant flow of carrier gas to flow through the pipe 8, and the sample in the reaction tank 4 is passed through the oxidizing agent and the acid, and the OC component derived from the OC component is 002 is passed through a water separator 14 and a dehumidifier 15 using a carrier gas to remove water and humidity, and then sent to a CO2 detector 17 to detect CO2.

d、予めT OOWJ度が既知の標準溶液でキャリブレ
ーションしておいて、データ処理器18により試料中の
f’001度が算出されプリンタなどに印字される。
d. Calibrate in advance with a standard solution with a known TOOWJ degree, and the data processor 18 calculates f'001 degree in the sample and prints it on a printer or the like.

上記の従来法でTOCを測定する場合は、単に酸化剤と
試料とを混合した後、加熱してTOC成分を酸化させ0
02 に変換して測定するだけなので、酸化剤、酸およ
びこれらを適切な精度に調製するのに用いる水に含まれ
る全炭素成分(TCりによる大きなブランク値が試料中
のTOOの測定値に加わる。このブランク値を小さくす
るには高純度の酸化剤、酸詔よび水を用いる必要があり
またこのように高純度のものを用いたとしても酸化剤溶
液の調製操作中に外部からの汚染により無視できない量
のToが検出される。したがって、従来は、試料を注入
せずに同様に測定操作を行うことにより予めブランク値
を求めこれを差引くことによって補正が行われる。
When measuring TOC using the conventional method described above, simply mix the oxidizing agent and the sample and then heat to oxidize the TOC component.
02, the total carbon content of the oxidizing agent, acid, and water used to prepare them with appropriate precision (a large blank value due to TC is added to the measured value of TOO in the sample). In order to reduce this blank value, it is necessary to use a highly pure oxidizing agent, acid powder, and water, and even if such highly purified oxidizing agents are used, there is a risk of contamination from the outside during the preparation of the oxidizing agent solution. A non-negligible amount of To is detected.Therefore, conventionally, correction is performed by performing a similar measurement operation without injecting a sample to obtain a blank value in advance and subtracting it.

しかし、例えば5%ペルオキソ硫酸カリウム2I11/
、10%リン酸0.6 dを使用した場合、これらの酸
化剤の含有するToに帰因するブランク値は約8μfに
なり、5回測定した場合の標準偏差は0.07μfとな
る。試料測定時には、このブランク値のばらつきが常に
加わるため、試料測定精度を低下させる大きな原因とな
る。例えば10m)1)mTOCの標準溶液をこの方法
で5回測定したときの相対標準偏差(C,V、 )は1
.04%になった。
However, for example, 5% potassium peroxosulfate 2I11/
, 0.6 d of 10% phosphoric acid, the blank value attributable to To contained in these oxidizing agents is about 8 μf, and the standard deviation when measured five times is 0.07 μf. When measuring a sample, variations in this blank value are always added, and this becomes a major cause of deterioration of sample measurement accuracy. For example, 10 m) 1) When a standard solution of mTOC is measured 5 times using this method, the relative standard deviation (C, V, ) is 1
.. It became 04%.

特に微量のTo(3測定を行なう場合には、その影響が
大きい。
This effect is particularly large when measuring a trace amount of To(3).

(ハ)問題点を解決するための手段 この発明は上記問題を改善するためになされたもので、
第1発明として無1炭素成分を含有せず有機炭素成分を
含有する水性試料に、酸化剤またはこれと紫外線を併用
して作用させて、試料中の有機炭素成分を二酸化炭素に
変換し、この二酸化炭素をキャリアガスによって排出さ
せて定量することにより全有機炭素を測定する方法にお
いて、予め、酸化剤酸性溶液を充分加熱しこの溶液が含
有する有機炭素成分を二酸化炭素に変換してこれをキャ
リアガスによって除去した後、試料を混合し、充分加熱
して試料中の有機炭素成分を二酸化炭素に変換しこの二
酸化炭素をキャリアガスによって排出させて定量するこ
とにより全有機炭素を測定することを特徴とする湿式酸
化式全有機炭素測定法を提供するものである。
(c) Means for solving the problems This invention was made to improve the above problems.
As a first invention, an oxidizing agent or a combination of the same and ultraviolet rays are applied to an aqueous sample containing an organic carbon component but not a carbon free component to convert the organic carbon component in the sample into carbon dioxide. In the method of measuring total organic carbon by exhausting carbon dioxide with a carrier gas and quantifying it, an acidic oxidizing agent solution is sufficiently heated in advance to convert the organic carbon component contained in this solution into carbon dioxide, and this is converted into a carrier gas. After removal by gas, the sample is mixed and sufficiently heated to convert the organic carbon components in the sample into carbon dioxide, and this carbon dioxide is discharged with a carrier gas and quantified to measure total organic carbon. This provides a wet oxidation total organic carbon measurement method.

この発明における試料は、ICを含有せずOCを含有す
る水性系試料であるが、試料がICとOCの両成分を含
有している場合は、IC成分を予め除去して測定試料と
される。IC成分は試料のpHを2〜4とすることによ
って容易に002に変換され、また実質的に002 を
含有しない窒素ガスなどでl1iIFcすることによっ
て、このCO2を容易に除去することができる7、なお
試料の量は一般に10μg〜10#/の範囲であり、高
濃度TOO試料では少な(低濃度TOOの試料で多く用
いられる。
The sample in this invention is an aqueous sample that does not contain IC but contains OC, but if the sample contains both IC and OC components, the IC component is removed in advance and the sample is used as a measurement sample. . The IC component is easily converted to 002 by adjusting the pH of the sample to 2 to 4, and this CO2 can be easily removed by IFc with nitrogen gas that does not substantially contain 0027. Note that the amount of sample is generally in the range of 10 μg to 10#/, and is small for high-concentration TOO samples (large amount is used for low-concentration TOO samples).

この発明に用いられる酸化剤としては従来用いられてい
るものでよく、ペルオキソ硫酸カリウムなどが挙げられ
る。またこの酸化剤の水溶液を酸性とするための酸も従
来用いられているものでよくリン酸や塩峻のような無機
酸が挙げられる。
The oxidizing agent used in this invention may be any conventionally used oxidizing agent, such as potassium peroxosulfate. Furthermore, the acid for making the aqueous solution of the oxidizing agent acidic may be any conventionally used acid, including inorganic acids such as phosphoric acid and sulfuric acid.

酸化剤と酸は一般に水溶液として用いられるが、酸化剤
として例えばペルオキソ硫酸カリウムを用いる場合は5
0〜10%水溶液、酸として例えばリン酸を用いるとき
は5〜15%水溶液が用いられる。
Oxidizing agents and acids are generally used as aqueous solutions, but when using potassium peroxosulfate as the oxidizing agent,
A 0 to 10% aqueous solution is used, and a 5 to 15% aqueous solution is used when, for example, phosphoric acid is used as the acid.

この発明では、まず酸化剤と酸との混合水溶液の酸化剤
酸性溶液を加熱し、その全炭素(To)をOOg  に
変換してこれを除去する。その加熱は約90〜100℃
で約3〜6分で充分である。一般に酸化剤は、加熱する
と酸化力が次第に減少するが、この程度の加熱では実用
上問題にならない。
In this invention, first, an acidic oxidizing agent solution, which is a mixed aqueous solution of an oxidizing agent and an acid, is heated to convert all the carbon (To) into OOg and remove it. The heating is about 90-100℃
Approximately 3 to 6 minutes is sufficient. Generally, when an oxidizing agent is heated, its oxidizing power gradually decreases, but this level of heating does not pose a practical problem.

加熱によって生成したOOg  はこの溶液に実質的に
CO2を含有しない窒素ガス、酸素ガス、精製空気など
のキャリアガスを通過曝気させてキャリアガスとともに
排出させて除去される。このキャリアガスは一般に50
〜150g//m程度で用いられる。
The OOg generated by heating is removed by aerating the solution through a carrier gas such as nitrogen gas, oxygen gas, purified air, etc. that does not substantially contain CO2, and discharging the solution together with the carrier gas. This carrier gas is generally 50%
It is used at about 150g//m.

次いでこのように処理してToを除去した酸化剤酸性溶
液と試料とを混合して前記のように加熱してそのOCを
CO2に変換して前記と同様にしてキャリアガスととも
に排出させて、そのC02をCO2検出器にて検出して
試料のTOCが算出される。
Next, the sample is mixed with the oxidizing agent acidic solution treated in this way to remove To, heated as described above to convert the OC to CO2, and discharged together with the carrier gas in the same manner as described above. TOC of the sample is calculated by detecting CO2 with a CO2 detector.

次にこの発明は、第2発明として、前記@1発明を実施
するための測定装置として、加熱炉が付1寓し排気口が
備えられた曝気槽、加熱炉が付属し試料注入口付きの反
応槽、水分離器、除湿器、およびデータ処理器が付属し
出口側に排気管路を備えた二酸化炭素検出器が管路で連
結され、酸化剤溶液槽から延出する送液用ポンプ付き送
液管路と、酸溶液槽から延出する送液用ポンプ付き送液
管路とが前記曝気槽に連結され、キャリアガス供給部か
ら延出する2本のバルブ付き管路の一方が前記l気水、
他方が前記反応槽にそれぞれ連結されてなり、最初に曝
気槽で酸化剤酸性溶液を加熱しキャリアガスで曝気して
その全炭素成分を二酸化炭素に変換して除去し、この溶
液と無機炭素成分を含まず有機炭素成分を含有する試料
とを混合して加熱して有機炭素成分を二酸化炭素に変換
してこれを検出して有機炭素量を算出しつるよう構成さ
れてなる湿式酸化式全有機炭素測定装置を提供するもの
である。
Next, this invention provides, as a second invention, a measuring device for carrying out the above-mentioned @1 invention, an aeration tank equipped with a heating furnace and an exhaust port, and an aeration tank equipped with a heating furnace and a sample injection port. A reaction tank, a water separator, a dehumidifier, and a data processor are attached, and a carbon dioxide detector with an exhaust line on the outlet side is connected by a pipe, and a pump for sending liquid extends from the oxidizer solution tank. A liquid sending pipe and a liquid sending pipe with a liquid sending pump extending from the acid solution tank are connected to the aeration tank, and one of the two valved pipes extending from the carrier gas supply section is connected to the l air water,
The other is connected to the reaction tank, and first, the oxidizing agent acidic solution is heated in the aeration tank and aerated with a carrier gas to convert all the carbon components into carbon dioxide and remove it, and this solution and the inorganic carbon component are A wet oxidation type all-organic system that is configured to mix a sample that does not contain carbon dioxide with a sample that contains an organic carbon component, heat it, convert the organic carbon component to carbon dioxide, detect this, and calculate the amount of organic carbon. The present invention provides a carbon measuring device.

まず曝気槽に前記酸化剤および酸溶液送液管路より送ら
れる酸化剤酸性溶液を注入し、槽の周囲に付属する加熱
炉で加熱して、溶液中のToをCO2に変換し、キャリ
アガス供給部から曝気槽に送られるキャリアガスを前記
溶液に通過曝気させて、曝気槽の排気口から外部に排出
させてCO2が除去される。
First, the oxidizing agent and the oxidizing agent acidic solution sent from the acid solution delivery pipeline are injected into the aeration tank, and heated in a heating furnace attached around the tank to convert To in the solution into CO2, and the carrier gas A carrier gas sent from the supply unit to the aeration tank is passed through the solution, aerated, and discharged to the outside from the exhaust port of the aeration tank to remove CO2.

このようにしてToを除去された前記溶液は反応槽に送
られ、次いで試料が添加される。次にこれを反応槽に付
属する加熱炉で加熱して試料中のOCをCO2に変換し
、反応槽に送られるキャリアガスによってこのCO2が
分離され、水分離器と除湿器を通過させて水分と湿分を
除去した後、CO2検出器に送られ検出測定され、デー
タ処理器によってTOC量が算出印字される。
The solution from which To has been removed in this way is sent to a reaction tank, and then a sample is added thereto. Next, this is heated in a heating furnace attached to the reaction tank to convert the OC in the sample into CO2, and this CO2 is separated by a carrier gas sent to the reaction tank, and then passed through a water separator and dehumidifier to remove moisture. After removing moisture, it is sent to a CO2 detector where it is detected and measured, and a data processor calculates and prints out the TOC amount.

上記曝気槽と反応槽は通常硬質ガラスあるいは石英ガラ
ス製のものが用いられる。また水分離器と除湿器として
は従来用いられているものが用いられ、C02検出器は
通常非分成形赤外線分析計(通常ピーク面積によって測
定される)が用いられる。試料、試薬、加熱条件、キャ
リアガスなどは前記したのと同様である。
The aeration tank and reaction tank are usually made of hard glass or quartz glass. Conventionally used water separators and dehumidifiers are used, and a non-separating infrared analyzer (usually measured by peak area) is used as the CO2 detector. The sample, reagent, heating conditions, carrier gas, etc. are the same as described above.

次に実施例によってこの発明を説明するが、この発明を
限定するものではない。
Next, the present invention will be explained by examples, but the present invention is not limited thereto.

に)実施例 まず第1図に示す装置を用いてこの発明の方法で測定す
る場合を順を追って説明する。
B) Example First, a case in which measurement is carried out by the method of the present invention using the apparatus shown in FIG. 1 will be explained step by step.

a 1. 一定量の酸化剤溶液と一定量の酸溶液とをそ
れぞれ酸化剤溶液槽8と酸溶液9とから定量ポンプ10
と11によって反応槽4に注入する。
a1. A metering pump 10 supplies a certain amount of oxidizing agent solution and a certain amount of acid solution from an oxidizing agent solution tank 8 and an acid solution 9, respectively.
and 11 into the reaction tank 4.

b 1.  加熱炉6を昇温して、反応槽4を約90〜
95℃で約3〜4分保持し、上記の酸化剤酸性溶液中の
TOを二酸化炭素に変換し昇温を停止する。
b1. The heating furnace 6 is heated to a temperature of about 90℃
The temperature is maintained at 95° C. for about 3 to 4 minutes to convert the TO in the oxidizing agent acidic solution to carbon dioxide, and then the temperature increase is stopped.

バルブ2を開いてキャリアガス供給部1より管路8を通
じてキャリアガスを反応槽4に送り、生成したC02 
をキャリアガスによって外部に排出する。次いでキャリ
アガスの供給を停止して反応槽4の温度を室温まで低下
させる。
The valve 2 is opened and the carrier gas is sent from the carrier gas supply section 1 to the reaction tank 4 through the pipe line 8, and the generated C02
is discharged to the outside by carrier gas. Next, the supply of the carrier gas is stopped and the temperature of the reaction tank 4 is lowered to room temperature.

c 1. 一定量の試料をマイクロシリンジ7を用いて
、試料注入口6を通じて反応槽4に注入する。
c1. A certain amount of sample is injected into the reaction tank 4 through the sample injection port 6 using the microsyringe 7 .

d 1.  加熱炉6を昇温しで反応槽4を約90〜9
5°Cで約3〜4分保持し、試料中のTOOを二酸化炭
素に変換した後これをキャリアガスで曝気することによ
って、水分離1114と除湿器16を通過させ水分と湿
分を除去してC02検出器の非分成形赤外線ガス分析計
17に送りC02を検出する。
d1. By raising the temperature of the heating furnace 6, the temperature of the reaction tank 4 is about 90~90℃.
After holding the sample at 5°C for about 3 to 4 minutes to convert TOO in the sample into carbon dioxide, the sample is aerated with a carrier gas and passed through a water separator 1114 and a dehumidifier 16 to remove water and moisture. The gas is then sent to the non-separating infrared gas analyzer 17 of the C02 detector to detect C02.

e l、  予めTOOd度が既知の標準溶液でキャリ
ブレーションして窓いて、データ処理器18により試料
中のTOOa度が算出されプリンタなどに印字される。
e l. The TOOa degree in the sample is calculated by the data processor 18 by calibrating and windowing with a standard solution whose TOOd degree is known in advance and printed on a printer or the like.

なお試料中のOC成分に揮発性(低沸点)のものがない
場合は上記b1におけるキャリアガスの停止と反応槽の
室温までの低下は行わずに01の操作に移ってもよい。
Note that if there is no volatile (low boiling point) OC component in the sample, the procedure may proceed to step 01 without stopping the carrier gas and lowering the temperature of the reaction tank to room temperature in step b1.

次に第2図に示すこの発明の測定装置の一実施例につい
て説明する。
Next, an embodiment of the measuring device of the present invention shown in FIG. 2 will be described.

a 2.  酸化剤水溶液と酸水溶液とを一定量づ\(
試料の一回の分析に使用されるfl)、酸化剤溶液槽8
0と酸溶液槽81とから定量ポンプ82と88(適当な
分注器でもよい)によって管路84と35を通じて曝気
槽37に送る(バルブ25と26は閉)。
a2. Add a certain amount of oxidizing agent aqueous solution and acid aqueous solution\(
fl) used for one analysis of the sample, oxidizing agent solution tank 8
0 and acid solution tank 81 by means of metering pumps 82 and 88 (which may be suitable dispensers) through lines 84 and 35 to aeration tank 37 (valves 25 and 26 closed).

b 2.  加熱炉38を昇温させて前記溶液を約95
℃で約4分間加熱する。その結果前記溶液中のToはC
O2に変換される。者8品、次にバルブ26を開いてキ
ャリアガス供給部21から管路24を通じてキャリアガ
スを曝気137に送り、前記溶液を通過・曝気させ排気
口39から排出し前記CO,を除去する。
b2. The temperature of the heating furnace 38 is increased to bring the solution to about 95%
Heat at ℃ for about 4 minutes. As a result, To in the solution is C
Converted to O2. Then, the valve 26 is opened to send the carrier gas from the carrier gas supply section 21 through the pipe 24 to the aeration 137, and the solution is passed through and aerated and discharged from the exhaust port 39 to remove the CO.

C2,バルブ26を開いて、加熱−曝気処理済の前記溶
液の全量を反応槽40に自然流下させる。
C2, open the valve 26 and allow the entire amount of the heated and aerated solution to flow down into the reaction tank 40.

d 2.  バルブ26を閉じ一定1の試料をマイクロ
シリンジ41で採取し試料注入口から反応槽40に注入
する(この操作は適当な自動試料注入器を用いてもよい
)。
d2. The valve 26 is closed, and a certain sample is taken with the microsyringe 41 and injected into the reaction tank 40 from the sample injection port (an appropriate automatic sample injector may be used for this operation).

e 2.  加熱7戸42を昇温して前記混合液48を
95°Cで約4分加熱する。その結果試料中のOCが(
”、02  に変換される。次にバルブ22を開いてキ
ャリアガス供給部21から管路28を通じて一定流、喰
に制御したキャリアガスを試料と前記溶液の混合液4B
内に通過曝気させる。生成したCO2はキャリアガスと
ともに水分離器45と除湿器46を通過して水分と湿分
が除去されCO2検出器48に送られCO2が検出され
、データ処理器49でOaZが算出され印字される、 なお第2図には記載していないが、CO2検出′a48
の前にCO2トラップ部を設置し、反応槽から送られる
C02 を一度このトラップでトラップした後、トラッ
プ部を加熱してCO2を放出して測定してもよい。この
優は第1図の装置についても同じことがいえる。
e2. The temperature of the heating unit 42 is raised to heat the mixed liquid 48 at 95° C. for about 4 minutes. As a result, the OC in the sample was (
Next, the valve 22 is opened and the carrier gas is supplied from the carrier gas supply section 21 through the pipe line 28 at a constant flow rate to the mixed liquid 4B of the sample and the solution.
Pass aeration inside. The generated CO2 passes through a water separator 45 and a dehumidifier 46 together with the carrier gas to remove water and humidity, and is sent to a CO2 detector 48 where CO2 is detected, and a data processor 49 calculates and prints OaZ. Although not shown in Figure 2, CO2 detection 'a48
A CO2 trap section may be installed in front of the reactor, and after the CO2 sent from the reaction tank is once trapped by this trap, the trap section may be heated to release CO2 for measurement. The same thing can be said about the device shown in FIG.

以上の実施例では酸化剤酸性溶液のTo成分量は零か零
に近いごく小さな値になるため測定精度が向上する。例
えば前記第1図の装置を用いて、この発明の方法で、前
記従来例と同様のi oppmTOCの標準溶液につい
て試験した結果、相対標準偏差は0.61%であった。
In the embodiments described above, the amount of To component in the oxidizing agent acidic solution is zero or a very small value close to zero, so that the measurement accuracy is improved. For example, when a standard solution of ioppmTOC similar to the conventional example was tested using the apparatus shown in FIG. 1 and the method of the present invention, the relative standard deviation was 0.61%.

(ホ)発明の効果 この発明によれば次のようなすぐれた効果が得られる。(e) Effects of the invention According to this invention, the following excellent effects can be obtained.

(1)酸化剤や酸によるブランク値がはゾゼロになるた
め測定精度が向上する。
(1) Measurement accuracy is improved because the blank value due to oxidizing agent or acid becomes zero.

(II)酸化剤や酸セよびその調製に使用する水にTC
成分が不純物として含まれていても影響しない。また調
製操作時における汚染に対する配慮が不要である。
(II) TC in the oxidizing agent, acid salt, and water used for its preparation.
Even if an ingredient is included as an impurity, it has no effect. Further, there is no need to consider contamination during preparation operations.

n++)ブランク値の測定および補正操作が不要である
n++) Blank value measurement and correction operations are not required.

GV)  酸化剤及び酸の溶液の注入量の精度が多少悪
くても測定直に影響しない(例えば10%程度の誤差は
影響しない)。
GV) Even if the accuracy of the injection amount of the oxidizing agent and acid solution is somewhat poor, it does not directly affect the measurement (for example, an error of about 10% does not affect it).

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

第1図は、従来用いられている湿式酸化式全有菌炭素測
定装置の構成説明図、第2図はこの発明の一実施例の湿
式峻化式全有1炭素測定装置の構成説明図である。 (1,21)・・・キャリア供給部、(8,80)・・
・酸化剤溶液槽、(9,81)・・・酸溶液槽、(7゜
41)・・・マイクロシリンジ、(4,40)・・・反
応1、(6,44)・・・試料注入口、(14,45)
・・・水分離器、(15,46)・・・除湿器、(17
゜48)・・・co2  検出器、(18,49)・・
・データ処理器。
FIG. 1 is an explanatory diagram of the configuration of a conventional wet oxidation type total sterile carbon measuring device, and FIG. 2 is a configuration explanatory diagram of a wet oxidation type total 1 carbon measuring device according to an embodiment of the present invention. be. (1,21)...Carrier supply section, (8,80)...
・Oxidizer solution tank, (9,81)...Acid solution tank, (7゜41)...Microsyringe, (4,40)...Reaction 1, (6,44)...Sample injection Entrance, (14,45)
...Water separator, (15,46) ...Dehumidifier, (17
゜48)...CO2 detector, (18,49)...
・Data processor.

Claims (1)

【特許請求の範囲】 1、無機炭素成分を含有せず有機炭素成分を含有する水
性試料に、酸化剤またはこれと紫外線を併用して作用さ
せて、試料中の有機炭素成分を二酸化炭素に変換し、こ
の二酸化炭素をキャリアガスによって排出させて定量す
ることにより全有機炭素を測定する方法において、予め
、酸化剤酸性溶液を充分加熱しこの溶液が含有する有機
炭素成分を二酸化炭素に変換してこれをキャリアガスに
よって除去した後、試料を混合し、充分加熱して試料中
の有機炭素成分を二酸化炭素に変換しこの二酸化炭素を
キャリアガスによって排出させて定量することにより全
有機炭素を測定することを特徴とする湿式酸化式全有機
炭素測定法。 2、加熱炉が付属し排気口が備えられた曝気槽、加熱炉
が付属し試料注入口付きの反応槽、水分離器、除湿器、
およびデータ処理器が付属し出口側に排気管路を備えた
二酸化炭素検出器が管路で連結され、酸化剤溶液槽から
延出する送液用ポンプ付き送液管路と、酸溶液槽から延
出する送液用ポンプ付合送液管路とが前記曝気槽に連結
され、キャリアガス供給部から延出する2本のバルブ付
き管路の一方が前記曝気槽に、他方が前記反応槽それぞ
れ連結されてなり、最 初に曝気槽で酸化剤酸性溶液を加熱しキャリアガスで曝
気してその全炭素成分を二酸化炭素に変換して除去し、
この溶液と無機炭素成分を含まず有機炭素成分を含有す
る試料とを混合して加熱して有機炭素成分を二酸化炭素
に変換してこれを検出して有機炭素量を算出しうるよう
構成されてなる湿式酸化式全有機炭素測定装置。
[Claims] 1. An oxidizing agent or a combination of the same and ultraviolet rays is applied to an aqueous sample containing an organic carbon component but not an inorganic carbon component to convert the organic carbon component in the sample into carbon dioxide. However, in the method of measuring total organic carbon by exhausting this carbon dioxide with a carrier gas and quantifying it, the oxidizing agent acidic solution is sufficiently heated in advance to convert the organic carbon component contained in this solution into carbon dioxide. After removing this with a carrier gas, the sample is mixed and heated sufficiently to convert the organic carbon component in the sample into carbon dioxide, and this carbon dioxide is exhausted with a carrier gas and quantified to measure total organic carbon. A wet oxidation total organic carbon measurement method characterized by: 2. Aeration tank with heating furnace and exhaust port, reaction tank with heating furnace and sample injection port, water separator, dehumidifier,
A carbon dioxide detector with a data processor attached and an exhaust pipe on the outlet side is connected by a pipe, and a liquid sending pipe with a liquid sending pump extending from the oxidizing agent solution tank and the acid solution tank. A liquid feeding pipe line with an extending liquid feeding pump is connected to the aeration tank, one of the two valved pipe lines extending from the carrier gas supply section is connected to the aeration tank, and the other is connected to the reaction tank. First, the oxidizer acidic solution is heated in an aeration tank and aerated with a carrier gas to convert all the carbon components into carbon dioxide and remove them.
This solution is mixed with a sample containing an organic carbon component but not an inorganic carbon component, and heated to convert the organic carbon component into carbon dioxide, which is detected to calculate the amount of organic carbon. A wet oxidation total organic carbon measuring device.
JP62006971A 1987-01-14 1987-01-14 Wet acid type total organic carbon measuring method and apparatus Pending JPS63173962A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP62006971A JPS63173962A (en) 1987-01-14 1987-01-14 Wet acid type total organic carbon measuring method and apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP62006971A JPS63173962A (en) 1987-01-14 1987-01-14 Wet acid type total organic carbon measuring method and apparatus

Publications (1)

Publication Number Publication Date
JPS63173962A true JPS63173962A (en) 1988-07-18

Family

ID=11653085

Family Applications (1)

Application Number Title Priority Date Filing Date
JP62006971A Pending JPS63173962A (en) 1987-01-14 1987-01-14 Wet acid type total organic carbon measuring method and apparatus

Country Status (1)

Country Link
JP (1) JPS63173962A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0316061U (en) * 1989-06-29 1991-02-18
JPH0375559A (en) * 1989-08-18 1991-03-29 Tokico Ltd Carbon-quantity measuring apparatus
CN103149250A (en) * 2013-03-04 2013-06-12 李熔 Online total organic carbon water quality analyzer and online total organic carbon water quality analyzing method

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0316061U (en) * 1989-06-29 1991-02-18
JPH0375559A (en) * 1989-08-18 1991-03-29 Tokico Ltd Carbon-quantity measuring apparatus
CN103149250A (en) * 2013-03-04 2013-06-12 李熔 Online total organic carbon water quality analyzer and online total organic carbon water quality analyzing method

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